CN102720553B - A kind of method and apparatus producing kinetic energy and refrigeration - Google Patents
A kind of method and apparatus producing kinetic energy and refrigeration Download PDFInfo
- Publication number
- CN102720553B CN102720553B CN201210127331.2A CN201210127331A CN102720553B CN 102720553 B CN102720553 B CN 102720553B CN 201210127331 A CN201210127331 A CN 201210127331A CN 102720553 B CN102720553 B CN 102720553B
- Authority
- CN
- China
- Prior art keywords
- working medium
- heat exchanger
- acting
- chamber
- steam state
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000005057 refrigeration Methods 0.000 title claims abstract description 31
- 238000000034 method Methods 0.000 title claims description 27
- 239000007788 liquid Substances 0.000 claims abstract description 86
- 239000006200 vaporizer Substances 0.000 claims abstract description 40
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 238000010521 absorption reaction Methods 0.000 claims abstract description 6
- 230000008859 change Effects 0.000 claims abstract description 3
- 230000008676 import Effects 0.000 claims description 55
- 238000009434 installation Methods 0.000 claims description 14
- 238000009835 boiling Methods 0.000 claims description 10
- 239000007791 liquid phase Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 3
- 238000011017 operating method Methods 0.000 claims 1
- 230000006835 compression Effects 0.000 abstract description 19
- 238000007906 compression Methods 0.000 abstract description 19
- 238000005516 engineering process Methods 0.000 abstract description 6
- 239000003507 refrigerant Substances 0.000 abstract 2
- 239000007789 gas Substances 0.000 description 11
- 230000006872 improvement Effects 0.000 description 11
- 230000008520 organization Effects 0.000 description 6
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 229910052786 argon Inorganic materials 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- 239000001307 helium Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 229910052743 krypton Inorganic materials 0.000 description 2
- DNNSSWSSYDEUBZ-UHFFFAOYSA-N krypton atom Chemical compound [Kr] DNNSSWSSYDEUBZ-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000035807 sensation Effects 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The present invention relates to the use of room temperature thermal source and produce kinetic energy and the technology of refrigeration and equipment, the technology contents of its power cycle is: the working medium after allowing the heat absorption in vaporizer (7) heat up enters decompressor (1) acting, compressor (3) is allowed to be compressed heating up and entering its interior steam state acting working medium through heat exchanger (2) A chamber after decompressor (1) does work, allow the above-mentioned steam state acting working medium having compressed intensification of its B intracavity flow out the steam state working medium heat release of decompressor (1) after the acting of its A intracavity with heat exchanger (2) again and produce liquid refrigerant, after the above-mentioned liquid refrigerant entered from heat exchanger (2) B chamber allowing main heat exchanger B intracavity again absorbs the heat of compression of steam state working medium compressing intensification from compressor (3) of its A intracavity, enter vaporizer (7).Above power cycle, only makes heat energy partially change into kinetic energy, without prejudice to thermodynamics first, two laws, is feasible.
Description
Technical field
The present invention relates to the use of room temperature thermal source to produce technical field and the apparatus field of kinetic energy and refrigeration, and use by
Energy and low-temperature receiver produced by kinetic energy that room temperature thermal source produces and the technology of refrigeration, make other material in liquid and its liquid
The technical field separated.The invention still further relates to utilize room temperature thermal source to produce the air-conditioning neck manufactured by the technology of kinetic energy and refrigeration
Territory.
Background technology
The energy kept in the Nature is diversified！And the energy relied primarily on the most in the world is fossil combustion
Material！The huge demand of the energy also makes it the most depleted in the world, is also dependent on consuming the side of the energy at refrigerating field simultaneously
Method manufactures low-temperature receiver, and this more exacerbates energy-intensive situation！People can produce the new technique of the energy in the exploration seek assiduously
With new equipment, also reduce, with what kind of technology and equipment, the energy resource consumption produced because manufacturing low-temperature receiver trying to explore！Application
Number providing for the patent of CN201110072380 and a kind of to allow room temperature thermal source to produce the technical scheme of kinetic energy and refrigeration, it allows steaming
Send out the acting working medium of the low boiling after room temperature thermal source absorbs heat in device (7) and enter decompressor (1) acting, then allow compressor (7)
Steam state acting working medium after entering its interior acting through heat exchanger (2) B chamber is compressed heating up, and recycling heat exchanger (2) allows
The steam state acting working medium compressing intensification in its B chamber is entered, after the acting of the uncompressed intensification of its A intracavity by compressor (3)
Steam state acting working medium heat release and be condensed into liquid acting working medium, then allow the liquid that working medium pump (5) condenses heat exchanger (2) B intracavity
State working medium carries out heat absorption and heats up in pumping into vaporizer (7)；Seem successfully from the power cycle of working medium of initially doing work several times, but because of pressure
The heat of compression of contracting machine (3) cannot be got rid of, and the temperature of the steam state acting working medium flowing through compressor (3) can be more and more higher, the most accumulative
The acting working medium heated up can reach its critical temperature and make power cycle be unable to maintain that.
Summary of the invention
Invention main heat exchanger (4) allows the liquid pumped out by working medium pump (5) acting working medium only absorb above-mentioned
Being exported that flow out by decompressor (1) and passing the steam state acting working medium that heat exchanger (2) enters in compressor (3) described in patent,
Because of the heat of compression produced by compressor (3) compression, thus provide a kind of method and apparatus producing kinetic energy and refrigeration, solve
The heat energy making room temperature thermal source be contained can not be transformed into kinetic energy and the problem not being provided that low-temperature receiver.
The heat energy contained by solving room temperature thermal source can not be transformed into kinetic energy and not be provided that the problem of low-temperature receiver, the present invention's
The enforcement step of the technical scheme of a kind of method producing kinetic energy and refrigeration is as follows:
[1] allow its boiling point in vaporizer (7) less than room temperature and time it is liquid phase liquid without superfluidity do work
The heat absorption of working medium heat source heats up；
[2] decompressor (1) allowing the acting working medium entrance heated up with thermal source heat exchange in vaporizer (7) be attached thereto does
Merit；
[3] the steam state acting working medium flowed out from decompressor (1) outlet after acting is allowed to enter behind heat exchanger (2) A chamber the most only to enter
Enter in compressor (3)；
[4] compressor (3) is allowed its interior steam state acting working medium of entrance to be compressed and makes it heat up；
[5] the steam state acting working medium having compressed intensification in compressor (3) is allowed to enter back into after entering main heat exchanger (4) A chamber
Heat exchanger (2) B chamber；
[6] allow at heat exchanger (2) B intracavity, because of condense to the acting working medium heat release of the steam state of heat exchanger (2) A intracavity
Liquid acting working medium enters working medium pump (5)；
[7] allow working medium pump (5) that the liquid acting working medium pump flowing into working medium pump (5) is entered main heat exchanger (4) B intracavity, and with
The acting working medium heat exchange of main heat exchanger (4) A intracavity and enter back into vaporizer (7) after heating up；
[8] procedure described above [1], [2], [3], [4], [5], [6], [7] it are repeated in.
In the above step [6], at heat exchanger (2) B intracavity, the steam state heated up by compression acting working medium is because of the temperature difference
Automatically carry out heat release, heat exchanger (2) to the follow-up steam state acting working medium exported from decompressor (1) of heat exchanger (2) A intracavity
The steam state heated up by the compression acting working medium of B intracavity produces liquid acting working medium, meanwhile, heat exchanger (2) A intracavity because of heat release
Steam state acting working medium is automatically absorbed heat because of the temperature difference intensification.
In the above step [7], the liquid at heat exchanger (2) B intracavity does work working medium through working medium pump (5) entrance master
While heat exchanger (4) B chamber, heat exchanger (2) A intracavity absorbed heat heat up steam state acting working medium enter compressor (3) carry out
Compression heats up, and compressor (3) is steam state acting working medium press-in main heat exchanger (4) the A intracavity further heated up because of compression；Leading
Heat exchanger (4) A intracavity the steam state compressed and further heat up acting working medium because of the temperature difference automatically to by working medium pump (5) pump
Enter the liquid acting working medium heat release of main heat exchanger (4) B intracavity, produce after the steam state acting working medium heat release of main heat exchanger (4) A intracavity
Raw liquid acting working medium and the working medium but uncooled steam state is done work of having lowered the temperature；Steam state acting working medium at main heat exchanger (4) A intracavity
While heat release, the working medium of doing work of the liquid at main heat exchanger (4) B intracavity is automatically absorbed heat because of the temperature difference intensification.
The step [3] repeated in the above step [8] is inner, is pressed by compressor (3) when heat exchanger (2) B intracavity has
During the acting working medium contracted and heat up, the steam state working medium of heat exchanger (2) A intracavity can be absorbed heat to the acting working medium of its B intracavity because of the temperature difference
And heat up.
The step [5] repeated in the above step [8] is inner, when main heat exchanger (4) B intracavity has working medium pump (5) institute
During the liquid acting working medium coming from the condensation of heat exchanger (2) B intracavity pumped into, the steam state acting working medium of main heat exchanger (4) A intracavity
Automatically become liquid acting working medium and lowered the temperature to the liquid acting working medium heat release of main heat exchanger (4) B intracavity because of the temperature difference
But uncooled steam state acting working medium, meanwhile, the liquid of main heat exchanger (4) B intracavity acting working medium is also absorbed heat because of the temperature difference intensification,
When liquid acting working medium and the working medium but uncooled steam state is done work of having lowered the temperature of main heat exchanger (4) A intracavity enter heat exchanger (2) B
During intracavity, the follow-up steam state acting working medium exported from decompressor (1) of heat exchanger (2) A intracavity, can only absorb at heat exchanger
(2) B intracavity all does work working medium, remaining after main heat exchanger (4) the A intracavity heat release heat of compression, and carries out and its institute
The heat absorbed heats up accordingly, and meanwhile, the liquid acting working medium flowing to heat exchanger (2) B intracavity can be lowered the temperature because of heat release, stream
Liquid acting working medium can be become to the cooling of heat exchanger (2) B intracavity but uncooled steam state acting working medium and drop the most further
Temperature is working medium but uncooled steam state is done work.
In the power cycle described in the technical program, with making the liquid at heat exchanger (2) its B intracavity can be because of self
Gravity and attitude that automatically export place, outflow heat exchanger (2) B chamber installation position is presented to the method installing heat exchanger (2),
The liquid acting working medium making the heat exchanger in above-described power cycle (2) its B intracavity automatically enters working medium pump (5)；With
The liquid at main heat exchanger (4) its A intracavity can be made because of self gravitation automatically to flow out export place, main heat exchanger (4) A chamber
The attitude that installation position is presented, to the method installing main heat exchanger (4), makes the main heat exchanger in above-described power cycle
(4) the liquid acting working medium of its A intracavity automatically enters the B chamber of heat exchanger (2).
If the heat exchange efficiency of the main heat exchanger (4) in the power cycle described in the technical program is below 50%, this skill
Power cycle described in art scheme then gradually can become to run because the heat of compression produced by compressor (3) can not get rid of.
If the heat exchange efficiency of the main heat exchanger (4) in the power cycle described in the technical program is 50%, this technical side
Heat exchanger (2) in power cycle described in case can continue heat exchange.If the master in the power cycle described in the technical program changes
The heat exchange efficiency of hot device (4) is between 50% and 100%, or 100%, and the steam state acting work that decompressor (1) exports
The temperature of matter be constant, there is no the interference of other thermals source such as the thermal source outside system and the frictional heat in equipment, the technical program
Heat exchanger (2) in described power cycle can taper off heat exchange, and the steam state in power cycle described in the technical program is done
Merit working medium is condensed into the process of liquid acting working medium and can gradually carry out at main heat exchanger (4) A intracavity.
In the power cycle of the acting working medium described in the technical program, flow out the steam state acting work that decompressor (1) exports
The temperature of matter is inversely proportional to the efficiency of the power cycle described in the technical program, the liquid acting of outflow heat exchanger (2) B chamber outlet
The density of working medium is directly proportional to the efficiency of the power cycle described in the technical program, the heat exchange efficiency of main heat exchanger (4) and this skill
The efficiency of the power cycle described in art scheme is directly proportional.
Its boiling point described in the technical program less than room temperature and time it is liquid phase liquid without superfluidity do work work
Matter is a kind of, as its boiling temperatures such as nitrogen, argon, krypton, carbon dioxide less than room temperature and time it is liquid phase without superfluidity
Liquid acting working medium.
Its boiling point described in the technical program refers to less than the superfluidity of the liquid acting working medium of room temperature: at its liquid
When certain low temperature, it can flow with undamped, such as helium II.
Power cycle described in the technical program, is simply kinetic energy a certain amount of heat energy portions turn, its sub-fraction
Energy is converted into frictional heat respectively and the heat of compression returns in vaporizer (7), its another fraction energy be converted into acoustic energy etc. other
Energy loss is fallen, so its power cycle is without departing from thermodynamics first, second law.
1. in order to solve after above-described power cycle stops, in the acting working medium import of vaporizer (7) to heat exchanger
(2) the pipeline between the outlet of B chamber and the liquid acting working medium of residual in equipment can absorb heat intensification, so under the influence of once
The problem of power cycle, on the basis of the technical scheme of a kind of above-mentioned method producing kinetic energy and refrigeration, is improved to: more than
After described power cycle terminates, allow secondary working medium pump (6) that the acting working medium import of vaporizer (7) to heat exchanger (2) B chamber is exported
Between the liquid acting working medium of residual pump into vaporizer (7) in.
2. in order to solve the impact of fixed gas in the power cycle described in above technical scheme or Technological improvement plan 1,
It is improved on the basis of power cycle described in above technical scheme or Technological improvement plan 1: allow fixed gas air pump (10) first
The power cycle of acting working medium is restarted after extracting the fixed gas in the device carrying out above-mentioned power cycle out；And allow fixed gas take out
The power cycle of air pump (10) acting working medium afterwards is extracted out the fixed gas needing to extract out in the device of power cycle.
3. in order to solve power cycle described in above technical scheme or Technological improvement plan 1 or Technological improvement plan 2
In the power cycle at initial stage, the temperature of the steam state acting working medium flowed out because of compressor (3) outlet is not less than its critical temperature and difficult
With the problem being liquefied, when flow out in compressor (3) the temperature of steam state acting working medium surmount the critical of steam state acting working medium
During temperature, allow low-temperature receiver (9) that the steam state acting working medium being exported between the outlet of main heat exchanger (4) A chamber from compressor (3) is dropped
Below the critical temperature of warm working medium of doing work to steam state.
Above-described low-temperature receiver (9) refers to refrigeration machine, or temperature meet power cycle requirement and its not with
Compressor (3) be exported to main heat exchanger (4) A chamber acting sender property outlet at acting working medium mix cold-storage medium, or
Be previously implanted main heat exchanger (4) B intracavity before above-mentioned power cycle starts, temperature meets the liquid that power cycle requires and does
Merit working medium.
Present invention also offers a kind of equipment producing kinetic energy and refrigeration, its organization plan is: it, by decompressor (1), changes
Hot device (2), compressor (3), main heat exchanger (4), working medium pump (5), its acting working medium import and its acting sender property outlet and
Its acting working medium is added mouth and is all equipped with vaporizer (7) composition controlling valve, and the acting sender property outlet connection of vaporizer (7) has swollen
The import of swollen machine (1), the outlet of decompressor (1) connects the A chamber import having heat exchanger (2), and the A chamber outlet of heat exchanger (2) connects
Having the import of compressor (3), the outlet of compressor (3) connects the A chamber import having main heat exchanger (4), the A chamber of main heat exchanger (4)
Outlet connection has the B chamber import of heat exchanger (2), and the B chamber outlet connection of heat exchanger (2) has the import of working medium pump (5), working medium pump
(5) outlet connects the B chamber import having main heat exchanger (4), and the B chamber outlet connection of main heat exchanger (4) has the acting of vaporizer (7)
Working medium import；The Installation posture of above-described heat exchanger (2) is: can make because of certainly at the liquid of heat exchanger (2) its B intracavity
Heavy sensation of the body power and attitude that automatically export place, outflow heat exchanger (2) B chamber installation position is presented；Above-described main heat exchanger
(4) Installation posture is: the liquid at main heat exchanger (4) its A intracavity can be made because of self gravitation automatically to flow out main changing
The attitude that export place, hot device (4) A chamber installation position is presented.
1. on the basis of the organization plan of above-described a kind of equipment producing kinetic energy and refrigeration, it is also possible to improve
For: the liquid acting working medium between the acting working medium import of vaporizer (7) exports to heat exchanger (2) B chamber can be because of self gravitation
And connect on the pipeline assembled and have the import of secondary working medium pump (6), the outlet of secondary working medium pump (6) connects the valvular vaporizer of peace
(7) residual liquid working medium import；The acting working medium import at vaporizer (7) described in this structure improvement project is to heat exchanger
(2) pipeline that the liquid acting working medium between the outlet of B chamber can be assembled because of self gravitation, refers in this structure improvement project institute
When the power cycle stated stops, the pipeline between acting working medium import to the B chamber of heat exchanger (2) of vaporizer (7) exports with
The liquid acting working medium not pumped into vaporizer (7) by working medium pump (5) in equipment, the pipe automatically can assembled because of self gravitation
Road.
2. in the organization plan of above-described a kind of equipment producing kinetic energy and refrigeration or its structure improvement project 1
On the basis of, it is also possible to it is improved to: connecting on the pipeline between the outlet of main heat exchanger (4) A chamber import to compressor (3) has not
Solidifying gas air pump (10).
3. in the organization plan of above-described a kind of equipment producing kinetic energy and refrigeration or its structure improvement project 1 or
On the basis of its structure improvement project 2, it is also possible to be improved to: at the acting sender property outlet of compressor (3) to main heat exchanger (4) A
Connect at the acting sender property outlet in chamber and have low-temperature receiver (9)..
The low-temperature receiver (9) described in structure improvement project 3 of above-described a kind of equipment producing kinetic energy and refrigeration refers to
Refrigeration machine, or temperature meet power cycle requirement and its not with compressor (3) be exported to main heat exchanger (4) A chamber
Acting sender property outlet at the cold-storage medium that mixes of acting working medium, or be previously implanted master before above-mentioned power cycle starts
Heat exchanger (4) B intracavity, temperature meet the liquid acting working medium that power cycle requires.
The invention has the beneficial effects as follows: by less energy loss, the heat contained by room temperature thermal source is made full use of,
And need not external low-temperature receiver, and also can freeze！The heat of compression produced by its compressor (3), and the mill that heat exchanger produces
In chafing, and other mechanical friction heat major part meeting Returning evaporimeter (7), people can break away from energy field and system from this
The dependence that Fossil fuel is produced by cold field, terminates the harm that natural environment is produced by combustion of fossil fuels！Further, according to heating power
Learn First Law, worldwide, if when energy field all uses the present invention with refrigerating field, the ring of the earth will not be made
It is colder that border becomes.
Accompanying drawing explanation
Fig. 1 is the enforcement block diagram of embodiment 1；
Fig. 2 is the structure chart of embodiment 2；
Fig. 3 is the enforcement block diagram of embodiment 3；
Fig. 4 is the structure chart of embodiment 4；
Fig. 5 is valve (11) and the structure chart of valve (8)；
Numeral in figure is expressed as:
1 is decompressor；2 is heat exchanger；3 is compressor；4 is main heat exchanger；5 is working medium pump；6 secondary working medium pumps；7 is that it does
Merit working medium import and its acting sender property outlet and its acting working medium are added mouth and residual liquid working medium import and are all pacified valvular
Vaporizer；8 is the control valve being positioned on the pipeline in parallel with between heat exchanger (2) B chamber import and the outlet of its B chamber；9 is cold
Source；10 is fixed gas air pump；11 is the control being positioned on the pipeline in parallel with between heat exchanger (2) A chamber import and the outlet of its A chamber
Valve processed.
Detailed description of the invention
Principle and feature to the present invention are described below, and example is served only for explaining the present invention, is not intended to limit
Determine the scope of the present invention.
Embodiment 1:
A kind of method producing kinetic energy and refrigeration, its technical scheme has 11 and implements step, and implementation step is:
[1] fixed gas air pump (10) is allowed to extract the pipeline of power cycle and the fixed gas needing to extract out in equipment out；
[2] allow its boiling point in vaporizer (7) less than room temperature and time it is liquid phase liquid without superfluidity do work
The heat absorption of working medium heat source heats up；
[3] decompressor (1) allowing the acting working medium entrance heated up with thermal source heat exchange in vaporizer (7) be attached thereto does
Merit；
[4] the steam state acting working medium flowed out from decompressor (1) outlet after acting is allowed to enter behind heat exchanger (2) A chamber the most only to enter
Enter in compressor (3)；
[5] compressor (3) is allowed to be compressed heating up entering its interior steam state acting working medium；
[6] the steam state acting working medium having compressed intensification in compressor (3) is allowed to enter back into after entering main heat exchanger (4) A chamber
Heat exchanger (2) B chamber.
[7] allow at heat exchanger (2) B intracavity, because of condense to the acting working medium heat release of the steam state of heat exchanger (2) A intracavity
Liquid acting working medium enters working medium pump (5)；
[8] allow working medium pump (5) that the liquid acting working medium pump flowing into working medium pump (5) is entered main heat exchanger (4) B intracavity, and with
The acting working medium heat exchange of main heat exchanger (4) A intracavity and enter back into vaporizer (7) after heating up；
[9] procedure described above [1], [2], [3], [4], [5], [6], [7], [8] it are repeated in；
[10] when the acting working medium of heat exchanger (2) A intracavity and the acting working medium of its B intracavity are without the temperature difference, regulate one with
Control valve (11) on pipeline in parallel between heat exchanger (2) A chamber import and the outlet of its A chamber, allows and exports from decompressor (1)
Acting working medium change to walk the pipeline in parallel with heat exchanger (2) A chamber and enter compressor (3)；Also regulation one and heat exchanger (2) B chamber
Control valve (8) on pipeline in parallel between import and the outlet of its B chamber, allows the acting work from the outlet of main heat exchanger (4) A chamber
Matter changes walks pipeline entrance working medium pump (5) in parallel with heat exchanger (2) B chamber；When doing in the pipeline in parallel with heat exchanger (2) A chamber
Merit working medium with and its B chamber pipeline in parallel in acting working medium have the temperature difference time, then regulate above-described two and control valves, carry
The flow of the acting working medium with its B intracavity of high pass heat exchanger (2) A intracavity.
[11] after power cycle stops, allowing secondary working medium pump (6) the acting working medium import of vaporizer (7) to heat exchanger
(2) the liquid acting working medium of the residual between the outlet of B chamber pumps in vaporizer (7).
Heat exchanger (2) B intracavity in the above step [7], the steam state heated up by compression acting working medium is because of the temperature difference certainly
Dynamicly carry out heat release, heat exchanger (2) B to the follow-up steam state acting working medium exported from decompressor (1) of heat exchanger (2) A intracavity
The steam state heated up by the compression acting working medium of intracavity produces liquid acting working medium, meanwhile, heat exchanger (2) A intracavity because of heat release
Steam state acting working medium is automatically absorbed heat because of the temperature difference intensification.
In the above step [8], the liquid at heat exchanger (2) B intracavity does work working medium through working medium pump (5) entrance master
While heat exchanger (4) B chamber, heat exchanger (2) A intracavity absorbed heat heat up steam state acting working medium enter compressor (3) carry out
Compression heats up, and compressor (3) is steam state acting working medium press-in main heat exchanger (4) the A intracavity further heated up because of compression；Leading
The steam state compressed and the further heat up acting working medium of heat exchanger (4) A intracavity automatically pumps into by working medium pump (5) because of the temperature difference
The liquid acting working medium heat release of main heat exchanger (4) B intracavity, produces after the steam state acting working medium heat release of main heat exchanger (4) A intracavity
Liquid acting working medium and the working medium but uncooled steam state is done work of having lowered the temperature；Steam state acting working medium at main heat exchanger (4) A intracavity is put
While heat, the working medium of doing work of the liquid at main heat exchanger (4) B intracavity is automatically absorbed heat because of the temperature difference intensification.
The step [4] repeated in the above step [9] is inner, is pressed by compressor (3) when heat exchanger (2) B intracavity has
During the acting working medium contracted and heat up, the steam state working medium of heat exchanger (2) A intracavity can be absorbed heat to the acting working medium of its B intracavity because of the temperature difference
And heat up.
The step [6] repeated in the above step [9] is inner, when main heat exchanger (4) B intracavity has working medium pump (5) institute
During the liquid acting working medium coming from the condensation of heat exchanger (2) B intracavity pumped into, the steam state acting working medium of main heat exchanger (4) A intracavity
Because of the temperature difference automatically to the liquid of main heat exchanger (4) B intracavity acting working medium heat release and become liquid acting working medium and lowered the temperature but
Uncooled steam state acting working medium, meanwhile, the liquid acting working medium of main heat exchanger (4) B intracavity also heats up because of temperature difference heat absorption, works as master
Liquid acting working medium and the working medium but uncooled steam state is done work of having lowered the temperature of heat exchanger (4) A intracavity enter heat exchanger (2) B intracavity
Time, the follow-up steam state acting working medium exported from decompressor (1) of heat exchanger (2) A intracavity, can only absorb in heat exchanger (2) B chamber
In all acting working medium, remaining after main heat exchanger (4) the A intracavity heat release heat of compression, and carry out being absorbed with it
Heat heats up accordingly, and meanwhile, the liquid acting working medium flowing to heat exchanger (2) B intracavity can be lowered the temperature because of heat release, flows to heat exchange
The cooling of device (2) B intracavity but uncooled steam state acting working medium can become liquid acting working medium and lower the temperature further but not
The steam state acting working medium of condensation.
With can make heat exchanger (2) its B intracavity liquid can because of self gravitation automatically outflow heat exchanger (2) B chamber
The attitude that export place installation position is presented, to the method installing heat exchanger (2), makes in the power cycle described in the present embodiment
The liquid acting working medium of heat exchanger (2) its B intracavity automatically enters working medium pump (5)；With making in its A chamber of main heat exchanger (4)
In liquid can automatically flow out the attitude that export place, main heat exchanger (4) A chamber installation position presented because of self gravitation and pacify
The method of dress main heat exchanger (4), makes the liquid of main heat exchanger (4) its A intracavity in the power cycle described in the present embodiment do work
Working medium automatically enters its B chamber of heat exchanger (2).
If the heat exchange efficiency of the main heat exchanger (4) in the power cycle described in the present embodiment is below 50%, this enforcement
Power cycle described in example then gradually can become to run because the heat of compression produced by compressor (3) can not get rid of.
If the heat exchange efficiency of the main heat exchanger (4) in the power cycle described in the present embodiment is 50%, the present embodiment institute
Heat exchanger (2) in the power cycle stated can continue heat exchange.If the main heat exchanger (4) in the power cycle described in the present embodiment
Heat exchange efficiency be between 50% and 100%, or 100%, and the temperature of steam state acting working medium that decompressor (1) exports
Be constant, there is no the interference of other thermals source such as the thermal source outside system and the frictional heat in equipment, the acting described in the present embodiment
Heat exchanger (2) in circulation can taper off heat exchange, and the steam state acting working medium in the power cycle described in the present embodiment is condensed into
The process of liquid acting working medium can gradually be carried out at main heat exchanger (4) A intracavity.
In the power cycle of the acting working medium described in the present embodiment, flow out the steam state acting working medium that decompressor (1) exports
The efficiency of temperature and the power cycle described in the present embodiment be inversely proportional to, the liquid acting working medium of outflow heat exchanger (2) B chamber outlet
Density be directly proportional to the efficiency of the power cycle described in the present embodiment, the heat exchange efficiency of main heat exchanger (4) and the present embodiment institute
The efficiency of the power cycle stated is directly proportional.
Its boiling point described in the present embodiment less than room temperature and time it is liquid phase liquid without superfluidity do work working medium
A kind of, as its boiling temperatures such as nitrogen, argon, krypton, carbon dioxide less than room temperature and time it is liquid phase without the liquid of superfluidity
State acting working medium.
Control valve (11) described in the present embodiment and control valve (8) are a kind of as it is shown in figure 5, have and control in it
The flow direction of fluid, and the valve of the flow of its interior fluid can be distributed；As it is shown in figure 1, they are arranged on its institute
The intersection that is connected with other pipelines of any one end of parallel pipeline.
Its boiling point described in the present embodiment refers to less than the superfluidity of the liquid acting working medium of room temperature: its liquid is in
During certain low temperature, it can flow with undamped, such as helium II.
Power cycle described in the present embodiment, is simply kinetic energy a certain amount of heat energy portions turn, its sub-fraction energy
Amount is converted into frictional heat respectively and the heat of compression returns in vaporizer (7), and its another fraction energy is converted into other energy such as acoustic energy
Amount lost, so its power cycle is without departing from thermodynamics first, second law.
Embodiment 2:
A kind of equipment producing kinetic energy and refrigeration, its organization plan is: it is by decompressor (1), heat exchanger (2), compressor
(3), main heat exchanger (4), working medium pump (5), secondary working medium pump (6), vaporizer (7), fixed gas air pump (10) forms, vaporizer
(7) acting sender property outlet connects the import having decompressor (1), and the outlet of decompressor (1) connects has the A chamber of heat exchanger (2) to enter
Mouthful, the A chamber outlet connection of heat exchanger (2) has the import of compressor (3), and the outlet of compressor (3) connects main heat exchanger (4)
The import of A chamber, the pipeline between the A chamber import being exported to main heat exchanger (4) of compressor (3) connects and has fixed gas air pump
(10) import, the A chamber outlet connection of main heat exchanger (4) has the B chamber import of heat exchanger (2), and the B chamber outlet of heat exchanger (2) is even
Being connected to the import of working medium pump (5), the B chamber of heat exchanger (2) is exported in the inlet ductwork of working medium pump (5) connect secondary working medium pump
(6) import, the outlet of secondary working medium pump (6) connects the residual liquid acting working medium import pacifying valvular vaporizer (7), work
The outlet of matter pump (5) connects the B chamber import having main heat exchanger (4), and the B chamber outlet connection of main heat exchanger (4) has vaporizer (7)
Acting working medium import；The Installation posture of above-described heat exchanger (2) is: can make the liquid meeting at heat exchanger (2) its B intracavity
The attitude that automatically export place, outflow heat exchanger (2) B chamber installation position is presented because of self gravitation；Above-described main heat exchange
The Installation posture of device (4) is: the liquid at main heat exchanger (4) its A intracavity can be made because of self gravitation automatically to flow out master
The attitude that export place, heat exchanger (4) A chamber installation position is presented；It is equipped with band valve on vaporizer (7) described in the present embodiment
Acting working medium import, band valve acting sender property outlet, residual liquid acting working medium import, the acting working medium of band valve of band valve
Interpolation mouth.
Embodiment 3:
A kind of method producing kinetic energy and refrigeration, the present embodiment is in place of the difference of embodiment 1: in embodiment 1 institute
In the power cycle at the initial stage of the power cycle stated, when in compressor (3) flow out steam state acting working medium temperature surmount vapour
State acting working medium critical temperature time, allow low-temperature receiver (9) the vapour being exported between main heat exchanger (4) A chamber import from compressor (3)
State acting working medium carries out being cooled to below the critical temperature of steam state acting working medium.
In the power cycle described in the present embodiment, the heat exchange efficiency of main heat exchanger (4) and the acting described in the present embodiment
The efficiency of circulation is directly proportional.
The present embodiment also can be improved to, before above-mentioned power cycle starts, appropriate temperature is met what power cycle required
Liquid acting working medium, injects main heat exchanger (4) B intracavity.
Embodiment 4:
A kind of equipment producing kinetic energy and refrigeration, the present embodiment is in place of the difference of embodiment 2: in embodiment 2 institute
In the organization plan of a kind of equipment producing kinetic energy and refrigeration stated, at the acting sender property outlet of compressor (3) to main heat exchanger
(4) the acting working medium import department in A chamber connects low-temperature receiver (9).
The present embodiment also can be improved to the acting sender property outlet at compressor (3) to the acting working medium in main heat exchanger (4) A chamber
It is connected on the pipeline of import department carry valvular liquid acting working medium liquid injection port.
Embodiment also can be improved at the acting sender property outlet in main heat exchanger (4) A chamber be connected to carry valvular liquid
Acting working medium liquid injection port.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all spirit in the present invention and
In principle, any modification, equivalent substitution and improvement etc. made, should be included within the scope of the present invention.
Claims (16)
1. the method producing kinetic energy and refrigeration, its operating procedure is:
[1] allow its boiling point in vaporizer (7) less than room temperature and time it is liquid phase liquid without superfluidity do work working medium
Heat source heat absorption heats up；
[2] allow the acting working medium heated up with thermal source heat exchange in vaporizer (7) enter the decompressor (1) being attached thereto do work；
[3] allow the steam state acting working medium flowed out from decompressor (1) outlet after acting enter behind heat exchanger (2) A chamber and only enter pressure again
In contracting machine (3)；
[4] compressor (3) is allowed its interior steam state acting working medium of entrance to be compressed and makes it heat up；
[5] the steam state acting working medium having compressed intensification in compressor (3) is allowed to enter back into heat exchange after entering main heat exchanger (4) A chamber
Device (2) B chamber；
[6] allow at heat exchanger (2) B intracavity, because of the liquid condensed to the acting working medium heat release of the steam state of heat exchanger (2) A intracavity
Acting working medium enters working medium pump (5)；
[7] allow working medium pump (5) that the liquid acting working medium pump flowing into working medium pump (5) is entered main heat exchanger (4) B intracavity, and change with main
The acting working medium heat exchange of hot device (4) A intracavity and enter back into vaporizer (7) after heating up；
[8] procedure described above [1], [2], [3], [4], [5], [6], [7] it are repeated in.
A kind of method producing kinetic energy and refrigeration the most according to claim 1, it is characterised in that: terminate at power cycle
After, allow secondary working medium pump (6) the liquid acting of the residual between vaporizer (7) acting working medium import to heat exchanger (2) B chamber outlet
Working medium pumps in vaporizer (7).
A kind of method producing kinetic energy and refrigeration the most according to claim 1, it is characterised in that: in power cycle, allow
The acting of acting working medium restarted by fixed gas air pump (10) after first extracting the fixed gas in the device carrying out above-mentioned power cycle out
Circulation；And allow in the device extracting power cycle in the power cycle of fixed gas air pump (10) acting working medium afterwards out
Need the fixed gas extracted out.
A kind of method producing kinetic energy and refrigeration the most according to claim 2, it is characterised in that: in power cycle, allow
The acting of acting working medium restarted by fixed gas air pump (10) after first extracting the fixed gas in the device carrying out above-mentioned power cycle out
Circulation；And allow in the device extracting power cycle in the power cycle of fixed gas air pump (10) acting working medium afterwards out
Need the fixed gas extracted out.
A kind of method producing kinetic energy and refrigeration the most according to claim 1, it is characterised in that: power cycle in the early stage
In, when flow out in compressor (3) the temperature of steam state acting working medium surmount the critical temperature of steam state acting working medium time, allow low-temperature receiver
(9) the steam state acting working medium being exported between the outlet of main heat exchanger (4) A chamber from compressor (3) is carried out being cooled to steam state acting
Below the critical temperature of working medium.
A kind of method producing kinetic energy and refrigeration the most according to claim 2, it is characterised in that: power cycle in the early stage
In, when flow out in compressor (3) the temperature of steam state acting working medium surmount the critical temperature of steam state acting working medium time, allow low-temperature receiver
(9) the steam state acting working medium being exported between the outlet of main heat exchanger (4) A chamber from compressor (3) is carried out being cooled to steam state acting
Below the critical temperature of working medium.
A kind of method producing kinetic energy and refrigeration the most according to claim 3, it is characterised in that: power cycle in the early stage
In, when flow out in compressor (3) the temperature of steam state acting working medium surmount the critical temperature of steam state acting working medium time, allow low-temperature receiver
(9) the steam state acting working medium being exported between the outlet of main heat exchanger (4) A chamber from compressor (3) is carried out being cooled to steam state acting
Below the critical temperature of working medium.
A kind of method producing kinetic energy and refrigeration the most according to claim 4, it is characterised in that: power cycle in the early stage
In, when flow out in compressor (3) the temperature of steam state acting working medium surmount the critical temperature of steam state acting working medium time, allow low-temperature receiver
(9) the steam state acting working medium being exported between the outlet of main heat exchanger (4) A chamber from compressor (3) is carried out being cooled to steam state acting
Below the critical temperature of working medium.
9. implementing an equipment for a kind of method producing kinetic energy and refrigeration as claimed in claim 1, wherein, it is by decompressor
(1), heat exchanger (2), compressor (3), main heat exchanger (4), working medium pump (5), go out in its acting working medium import and its acting working medium
Mouth and its acting working medium are added mouth and are all pacified valvular vaporizer (7) composition, and the acting sender property outlet of vaporizer (7) connects to be had
The import of decompressor (1), the outlet of decompressor (1) connects has the liquid in making its B intracavity can because of self gravitation automatically
Flowing out the A chamber import of the heat exchanger (2) of the attitude installation of its B chamber outlet, the A chamber outlet of above-described heat exchanger (2) connects
Having the import of compressor (3), the outlet of compressor (3) connects has the liquid in making its A intracavity can be automatic because of self gravitation
Ground flows out the A chamber import of the main heat exchanger (4) of the attitude installation of its A chamber outlet, in the A chamber of above-described main heat exchanger (4)
Outlet connection has the B chamber import of above-described heat exchanger (2), and the B chamber outlet connection of above-described heat exchanger (2) has working medium
The import of pump (5), the outlet of working medium pump (5) connects the B chamber import having above-described main heat exchanger (4), above-described
The B chamber outlet connection of main heat exchanger (4) has the acting working medium import of vaporizer (7).
Equipment the most according to claim 9, it is characterised in that: in the acting working medium import of vaporizer (7) to heat exchanger
(2), between the outlet of B chamber, can make to connect on the liquid acting pipeline assembled because of self gravitation of working medium have secondary working medium pump (6)
Import, the outlet of secondary working medium pump (6) connects the residual liquid acting working medium import pacifying valvular vaporizer (7).
11. equipment according to claim 9, it is characterised in that: in main heat exchanger (4) A chamber import going out to compressor (3)
Connect on pipeline between Kou and have fixed gas air pump (10).
12. equipment according to claim 10, it is characterised in that: in main heat exchanger (4) A chamber import to compressor (3)
Connect on pipeline between outlet and have fixed gas air pump (10).
13. equipment according to claim 9, it is characterised in that: at the acting sender property outlet of compressor (3) to main heat exchanger
(4) at the acting sender property outlet in A chamber, connection has low-temperature receiver (9).
14. equipment according to claim 10, it is characterised in that: at the acting sender property outlet of compressor (3) to main heat exchange
Connect at the acting sender property outlet in device (4) A chamber and have low-temperature receiver (9).
15. equipment according to claim 11, it is characterised in that: at the acting sender property outlet of compressor (3) to main heat exchange
Connect at the acting sender property outlet in device (4) A chamber and have low-temperature receiver (9).
16. equipment according to claim 12, it is characterised in that: at the acting sender property outlet of compressor (3) to main heat exchange
Connect at the acting sender property outlet in device (4) A chamber and have low-temperature receiver (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210127331.2A CN102720553B (en) | 2012-04-27 | 2012-04-27 | A kind of method and apparatus producing kinetic energy and refrigeration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210127331.2A CN102720553B (en) | 2012-04-27 | 2012-04-27 | A kind of method and apparatus producing kinetic energy and refrigeration |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102720553A CN102720553A (en) | 2012-10-10 |
| CN102720553B true CN102720553B (en) | 2016-12-14 |
Family
ID=46946400
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210127331.2A Active CN102720553B (en) | 2012-04-27 | 2012-04-27 | A kind of method and apparatus producing kinetic energy and refrigeration |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102720553B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6196341A (en) * | 1984-10-17 | 1986-05-15 | Kajima Corp | Transporting method of air conditioning heat energy |
| JPH09126567A (en) * | 1995-10-27 | 1997-05-16 | Yamaha Motor Co Ltd | Air conditioner |
| CN101586482A (en) * | 2008-05-23 | 2009-11-25 | 雷衍章 | Low-temperature type engine and heat regenerating method thereof |
| CN201463409U (en) * | 2009-07-14 | 2010-05-12 | 沃姆制冷设备(上海)有限公司 | Transcritical turbulent circulation system for carbon dioxide heat pump unit |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102005024685A1 (en) * | 2004-05-31 | 2005-12-29 | Denso Corp., Kariya | heat circuit |
-
2012
- 2012-04-27 CN CN201210127331.2A patent/CN102720553B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6196341A (en) * | 1984-10-17 | 1986-05-15 | Kajima Corp | Transporting method of air conditioning heat energy |
| JPH09126567A (en) * | 1995-10-27 | 1997-05-16 | Yamaha Motor Co Ltd | Air conditioner |
| CN101586482A (en) * | 2008-05-23 | 2009-11-25 | 雷衍章 | Low-temperature type engine and heat regenerating method thereof |
| CN201463409U (en) * | 2009-07-14 | 2010-05-12 | 沃姆制冷设备(上海)有限公司 | Transcritical turbulent circulation system for carbon dioxide heat pump unit |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102720553A (en) | 2012-10-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103629860B (en) | Trans-critical cycle CO 2cool and thermal power combined cycle system | |
| CN106895603B (en) | Compression/absorption enclosed parallel connection composite fuel gas heat pump system operation method | |
| CN104676943B (en) | CO2 high-temperature heat pump system | |
| CN105324616A (en) | Oil recovery for refrigeration system | |
| CN101851945A (en) | Device for preparing liquid water by air | |
| CN106871479A (en) | A kind of cold recovery formula varying capacity air source heat pump system | |
| CN206056012U (en) | Realize the heat cascade utilization heat pump of cold and heat combined supply | |
| CN104896793A (en) | Air conditioner water heater system | |
| CN105570988B (en) | Air conditioner and control method thereof | |
| CN105157274B (en) | cooling/heating system | |
| CN105588365B (en) | A kind of heat-flash type outdoor unit, heat pump system and its control method | |
| CN108007003A (en) | Two-stage Compression air source heat pump system | |
| CN206755651U (en) | Compression/absorption enclosed parallel connection composite fuel gas heat pump assembly | |
| CN102720553B (en) | A kind of method and apparatus producing kinetic energy and refrigeration | |
| CN205783983U (en) | The heat high efficiente callback device of air source handpiece Water Chilling Units | |
| CN207922617U (en) | A kind of heat pump system with drip tray ice-melt pipeline | |
| CN205505518U (en) | Five kinds of mode's air conditioner heat pump device | |
| CN204006769U (en) | Two stages of compression continuously heating device | |
| CN104676940B (en) | A kind of Two-stage Compression air source heat pump system | |
| CN204240587U (en) | Based on the solar heat-pump water heater system under variable refrigerant volume multiplex system form | |
| CN106225305A (en) | First kind thermal drivers compression absorption heat pump | |
| CN106907936B (en) | The gas burning system of multiple cooling and warming output | |
| CN206056043U (en) | The hot fluorine defrosting system of refrigeration unit | |
| CN104132473A (en) | Two-stage compression uninterruptible heating device and two-stage compression uninterruptible heating defrosting method | |
| KR102010687B1 (en) | Heat Pump Hot Water System |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| DD01 | Delivery of document by public notice |
Addressee: Wang Fawen Document name: Notification to Pay the Fees |
|
| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: Wang Fawen Document name: Notification to Pay the Fees |
|
| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: Wang Fawen Document name: payment instructions |
|
| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: Wang Fawen Document name: payment instructions |
|
| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: Wang Fawen Document name: payment instructions |
|
| DD01 | Delivery of document by public notice |