CN104180690B - A kind of new liquid intensification gasification installation and method of work - Google Patents
A kind of new liquid intensification gasification installation and method of work Download PDFInfo
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- CN104180690B CN104180690B CN201410415246.5A CN201410415246A CN104180690B CN 104180690 B CN104180690 B CN 104180690B CN 201410415246 A CN201410415246 A CN 201410415246A CN 104180690 B CN104180690 B CN 104180690B
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- 239000007788 liquid Substances 0.000 title claims abstract description 126
- 238000002309 gasification Methods 0.000 title claims abstract description 38
- 238000009434 installation Methods 0.000 title claims abstract description 17
- 238000000034 method Methods 0.000 title claims abstract description 15
- 230000000694 effects Effects 0.000 claims abstract description 10
- 230000008016 vaporization Effects 0.000 claims description 21
- 239000012530 fluid Substances 0.000 claims description 17
- 238000010521 absorption reaction Methods 0.000 claims description 16
- 238000009834 vaporization Methods 0.000 claims description 16
- 238000000889 atomisation Methods 0.000 claims description 9
- 230000009471 action Effects 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 5
- 238000009835 boiling Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 230000001002 morphogenetic effect Effects 0.000 claims description 3
- 230000008901 benefit Effects 0.000 description 4
- 230000008859 change Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Abstract
The invention discloses a kind of new liquid intensification gasification installation and method of work, a kind of new liquid intensification gasification installation wherein, comprising: the outlet of gasifier, thermal source liquid, the outlet of gasified liquid entrance, thermal source liquid entrance and eddy current high-temperature gas; Described thermal source liquid outlet connects gasifier; Described gasified liquid entrance is arranged on gasifier outside; Described thermal source liquid entrance connects gasifier; Described eddy current high-temperature gas outlet is arranged on gasifier outside; Vacuum generator, muffler, vacuum generator outlet, the first connector, thin heat exchanger tube, the second connector, middle heat exchanger tube, the 3rd connector, thick heat exchanger tube, the 4th connector, gradient tube and vortex tube is provided with in described gasifier.The present invention utilizes the cold and hot separating effect of the air-flow of vortex tube, makes the output gas temperature after gasifying higher than the temperature of thermal source liquid, can further increase heat exchange efficiency.
Description
Technical field
the present invention relates to liquid intensification gasification installation, be specifically related to a kind of new liquid intensification gasification installation and method of work.
Background technology
Traditional liquid gasification device progressively gasifies from liquid state to gas, and the temperature difference reduces gradually, and heat exchanger effectiveness is low; Heat exchange is uneven, and frosting, frozen phenomenon easily appear in gasifier internal-external heat exchanger position; Simultaneously due to heat conducting delay, the gas temperature of general final output is at least lower than thermal source about 5 degrees Celsius.Efficient heat exchange efficiency can not be reached.
Summary of the invention
The present invention is according to fluid mechanics principle, the kinetic energy of the liquid gas utilizing entrance to be gasified, the gas and vapor permeation that suction part has gasified, realize physics atomization and preliminary vaporization, make liquid gas to be gasified keep lower temperature as far as possible in heat absorption vaporization, gasification, keep the larger temperature difference with thermal source, thus there is heat absorption capacity large as far as possible, and make heat exchange even, improve heat exchange efficiency.Compressible fluid in fluid mechanics principle is also utilized to increase when stream tube section is long-pending, flow velocity can be caused to decline, temperature declines, the principle that pressure reduces, the gas in heat exchange is made to keep lower temperature as far as possible by increasing line cross section (stream tube section), keep the larger temperature difference as far as possible, improve heat absorption capacity to greatest extent.Finally make vaporization, the gas of gasification has higher temperature, higher pressure under equal thermal source condition.
Further, utilize the property of vortex tube, the gas of gasification is divided into colder, hotter two strands of air-flows further by vortex tube, thermal current exports; Cold airflow returns vacuum generator through return duct, enters recuperated cycle again, at utmost draws the temperature of thermal source, at utmost promotes the gas temperature of output, make export gas temperature can higher than the temperature of heat exchange thermal source.
According to an aspect of the present invention, provide a kind of new liquid intensification gasification installation, comprising: the outlet of gasifier, thermal source liquid, the outlet of gasified liquid entrance, thermal source liquid entrance and eddy current high-temperature gas; Described thermal source liquid outlet connects gasifier; Described gasified liquid entrance is arranged on gasifier outside; Described thermal source liquid entrance connects gasifier; Described eddy current high-temperature gas outlet is arranged on gasifier outside; Vacuum generator, muffler, vacuum generator outlet, the first connector, thin heat exchanger tube, the second connector, middle heat exchanger tube, the 3rd connector, thick heat exchanger tube, the 4th connector, gradient tube and vortex tube is provided with in described gasifier; Described gasified liquid entrance connects vacuum generator; Described vacuum generator connects vacuum generator outlet; Described muffler connects vacuum generator; Described vacuum generator outlet connection first connector; Described first connector connects thin heat exchanger tube; Described thin heat exchanger tube connects the second connector; Heat exchanger tube during described second connector connects; Described middle heat exchanger tube connects the 3rd connector; Described 3rd connector connects thick heat exchanger tube; Described thick heat exchanger tube connects the 4th connector; Described 4th connector connects gradient tube; Described gradient tube connects vortex tube; Described vortex tube connects the outlet of eddy current high-temperature gas and muffler respectively.
According to another aspect of the invention, provide a kind of new liquid intensification gasification installation method of work, comprise the following steps:
S1, described thermal source liquid entrance input thermal source liquid;
S2, is input to vacuum generator liquid to be gasified from gasified liquid entrance with pump;
S3, the morphogenetic jet drive surrounding liquid of liquid that described vacuum generator is to be vaporized or gas flow together, vacuum action is formed, thus by the gas that pipeline suction part has gasified, with jet mixing at muffler, gas temperature declines, the heat-transmission of portion gas disengaged vapor makes fluid temperature rise, a part of liquid gasification, different according to the gas temperature sucked from muffler, institute's heat content is different, forms atomization, vaporization, gasification result;
S4, to be exported by vacuum generator export along with jet and muffler suction gas is mixed to form vaporific or vaporous or the gas that is gasified totally in described vacuum generator;
S5, the fog-like liquid that the outlet of described vacuum generator exports or vaporous liquid or gas output to thin heat exchanger tube by the first connector;
S6, be in the liquid gas of gaseous state or the lower vaporization of temperature or atomization, enter in thin heat exchanger tube with vaporific or vaporous or gas form, along with outer wall and be full of thermal source liquid institute heat content in gasifier import heat exchange in pipeline into, the inside is still in liquid liquid and comes to life vaporization, the gas heating vaporize, gasified, along with boiling, along with intensification, volumetric expansion, become compressible fluid by the incompressible fluid of liquid state, pressure raises, and temperature is close to the hydrothermal sources providing heat outside tube wall;
S7, the liquid of gasification enters into after cross-sectional area increase heat exchanger tube through the second connector, because realizing expanding, pressure drop, temperature declines, in pipeline, gas and pipeline external heat source liquid temperature difference increase, heat absorption capacity increases, and continues to heat up, and pressure progressively gos up, pipeline internal-external temperature difference moves closer to, and trends towards balance heat transfer; Thick heat exchanger tube is entered into again by the 3rd connector, heat exchanging pipe area increases again, the gas pressure of gasify in pipeline, vaporizing declines again, temperature declines again, increase with pipeline external heat source liquid temperature difference, heat absorption capacity increases, and continues again heat absorption and heats up, heat absorption boosting, then outputs to connection gradient tube by the 4th connector;
S8, passing through connection gradient tube, pipeline area progressively reduces, pressure progressively increases, and temperature rises, and reaches or can a little more than the temperature of thermal source liquid, then enter vortex tube, by the one-to-two again of air-flow in vortex tube, export higher temperature gas and lower temperature gas respectively; The gas of high temperature is exported by the outlet of eddy current high-temperature gas; Another part comparatively cryogenic gas backs vacuum generator from the outlet of eddy current cryogenic gas by muffler, again mixes in vacuum generator;
S9, enters next working cycles.
Further, described step S4 is specially: when treating that gasifying liquid flow is less, and the heat energy that the return-air sucked by jet vacuum action is carried is not enough to the liquid mixed with it is vaporized, and just forms misty liquid droplets; When gasifier flow is very little, amount of jet is very little, and it is very little that muffler produces the effect vacuumized, and the rotary speed that vortex tube gas forms eddy current is very low, do not have eddy current to be separated the effect of hot and cold air, in pipeline, liquid gasification process is close or identical with traditional gasifier.
Advantage of the present invention:
The present invention utilizes the kinetic energy of fluid to make evaporimeter internal working medium shuttling movement, accelerates heat exchange, makes heat exchange even;
The gas of vaporizing, gasifying utilizing the fluidic architecture of vacuum generator to introduce of the present invention, the temperature different according to thermal source liquid, suction temperature is different, with liquid state can produce after bog mixes that physics is atomized, vaporizes, gasify different-effect, and through heat hybrid switching, make it major part vaporization, such ultralow temperature gas specific heat is less, temperature is lower, contacts evenly with heat exchange tube wall, and the large temperature difference improves heat exchange efficiency;
The pipeline (gas flow pipe) of the present invention's design is from carefully to slightly, although constantly absorb heat, but the volume expansion of flowing, pressure drop can occur, temperature reduces, thus can create the larger temperature difference as far as possible and absorb heat, close up at export pipeline, cross-sectional area reduces (stream pipe attenuates), causes the gas boost gasified of flowing to heat up, make the gas after the gasification of discharging have maximum pressure and temperature, improve heat exchange efficiency.When not having gas to flow, be then equivalent to common gasifier, static gas flow pipe change does not have the effect of lifting pressure, lifting temperature; The rotary speed that vortex tube gas forms eddy current is very low, and do not have eddy current to be separated the effect of hot and cold air, in pipeline, liquid gasification process is close or identical with traditional gasifier.
Except object described above, feature and advantage, the present invention also has other object, feature and advantage.Below with reference to figure, the present invention is further detailed explanation.
Accompanying drawing explanation
The accompanying drawing forming a application's part is used to provide a further understanding of the present invention, and schematic description and description of the present invention, for explaining the present invention, does not form inappropriate limitation of the present invention.
Fig. 1 is a kind of new liquid intensification gasification installation structural representation of the present invention;
Fig. 2 is a kind of new liquid intensification gasification installation method of work flow chart of the present invention.
Description of reference numerals:
1 for gasifier, 2 for thermal source liquid outlet, 3 for gasified liquid entrance, 4 for thermal source liquid entrance, 5 for eddy current high-temperature gas outlet, 6 for vacuum generator, 7 for muffler, 8 for vacuum generator outlet, 9 be the first connector, 10 for thin heat exchanger tube, 11 be the second connector, 12 for middle heat exchanger tube, 13 be the 3rd connector, 14 for thick heat exchanger tube, 15 be the 4th connector, 16 for gradient tube and 17 be vortex tube, 18 be eddy current cryogenic gas delivery outlet, 19 be vortex tube inlet.
Detailed description of the invention
In order to make object of the present invention, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the present invention is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the present invention, be not intended to limit the present invention.
Embodiment 1
Fig. 1 shows a kind of new liquid intensification gasification installation structural representation of the present invention.
With reference to figure 1, a kind of new liquid intensification gasification installation as shown in Figure 1, comprising: gasifier 1, thermal source liquid outlet 2, gasified liquid entrance 3, thermal source liquid entrance 4 and eddy current high-temperature gas outlet 5; Described thermal source liquid outlet 2 connects gasifier 1; It is outside that described gasified liquid entrance 3 is arranged on gasifier 1; Described thermal source liquid entrance 4 connects gasifier 1; It is outside that described eddy current high-temperature gas outlet 5 is arranged on gasifier 1; Vacuum generator 6, muffler 7, vacuum generator outlet the 8, first connector 9, thin heat exchanger tube 10, second connector 11, middle heat exchanger tube 12, the 3rd connector 13, thick heat exchanger tube 14, the 4th connector 15, gradient tube 16 and vortex tube 17 is provided with in described gasifier 1; Described gasified liquid entrance 3 connects vacuum generator 6; Described vacuum generator 6 connects vacuum generator outlet 8; Described muffler 7 connects vacuum generator 6; Described vacuum generator outlet 8 connects the first connector 9; Described first connector 9 connects thin heat exchanger tube 10; Described thin heat exchanger tube 10 connects the second connector 11; Heat exchanger tube 12 during described second connector 11 connects; Described middle heat exchanger tube 12 connects the 3rd connector 13; Described 3rd connector 13 connects thick heat exchanger tube 14; Described thick heat exchanger tube 14 connects the 4th connector 15; Described 4th connector 15 connects gradient tube 16; Described gradient tube 16 connects vortex tube 17; Described vortex tube 17 connects eddy current high-temperature gas outlet 5 and muffler 7 respectively.
Embodiment 2
Fig. 2 shows a kind of new liquid intensification gasification installation method of work flow chart of the present invention.
With reference to figure 2, as shown in Figure 2, a kind of new liquid intensification gasification installation method of work, comprises the following steps:
S1, described thermal source liquid entrance 4 inputs thermal source liquid;
S2, is input to vacuum generator 6 liquid to be gasified from gasified liquid entrance 3 with pump;
S3, the morphogenetic jet drive surrounding liquid of liquid that described vacuum generator 6 is to be vaporized or gas flow together, vacuum action is formed, thus by the gas that pipeline suction part has gasified, with jet mixing at muffler 7, gas temperature declines, the heat-transmission of portion gas disengaged vapor makes fluid temperature rise, a part of liquid gasification, different according to the gas temperature sucked from muffler 7, institute's heat content is different, forms atomization, vaporization, gasification result;
S4, exports 8 by vacuum generator export along with jet and muffler 7 suction gas is mixed to form vaporific or vaporous or the gas that is gasified totally in described vacuum generator 6;
S5, described vacuum generator exports 8 fog-like liquids exported or vaporous liquid or gas and outputs to thin heat exchanger tube 10 by the first connector 9;
S6, be in the liquid gas of gaseous state or the lower vaporization of temperature or atomization, enter in thin heat exchanger tube 10 with vaporific or vaporous or gas form, along with outer wall and be full of thermal source liquid institute heat content in gasifier import heat exchange in pipeline into, the inside is still in liquid liquid and comes to life vaporization, the gas heating vaporize, gasified, along with boiling, along with intensification, volumetric expansion, become compressible fluid by the incompressible fluid of liquid state, pressure raises, and temperature is close to the hydrothermal sources providing heat outside tube wall;
S7, the liquid of gasification enters into after cross-sectional area increase heat exchanger tube 12 through the second connector 11, because realizing expanding, pressure drop, temperature declines, in pipeline, gas and pipeline external heat source liquid temperature difference increase, heat absorption capacity increases, and continues to heat up, and pressure progressively gos up, pipeline internal-external temperature difference moves closer to, and trends towards balance heat transfer; Thick heat exchanger tube 14 is entered into again by the 3rd connector 13, heat exchanging pipe area increases again, the gas pressure of gasify in pipeline, vaporizing declines again, temperature declines again, increase with pipeline external heat source liquid temperature difference, heat absorption capacity increases, and continues again heat absorption and heats up, heat absorption boosting, is then outputted to by the 4th connector 15 and connects gradient tube 16;
S8, in time connecting gradient tube (16), pipeline area progressively reduces, pressure progressively increases, temperature rises, and reaches or a little more than the temperature of thermal source liquid, can then enter vortex tube (17), by vortex tube (17) interior air-flow one-to-two again, export higher temperature gas and lower temperature gas respectively; The gas of high temperature is exported by eddy current high-temperature gas outlet (5); Another part comparatively cryogenic gas backs vacuum generator (6) from eddy current cryogenic gas outlet (18) by muffler (7), again mixes in vacuum generator (6);
S9, enters next working cycles.
Described step S4 is specially: when treating that gasifying liquid flow is less, and the heat energy that the return-air sucked by jet vacuum action is carried is not enough to the liquid mixed with it is vaporized, and just forms misty liquid droplets; When gasifier flow is very little, amount of jet is very little, and it is very little that muffler produces the effect vacuumized, and in pipeline, liquid gasification process is close or identical with traditional gasifier.
The present invention utilizes the kinetic energy of fluid to make evaporimeter internal working medium shuttling movement, as far as possible rapid atomization, vaporization, gasification, and specific heat reduces, temperature is lower, heat exchange is even; The gas of having vaporized that fluidic architecture (vacuum generator) is introduced, liquid towards treat that bog carries out physics atomization, and through heat exchange, make it major part vaporization; The pipeline (gas flow pipe) of design, from carefully to slightly, closes up at export pipeline, more from coarse to fine, causes gas to heat, boosts, improve the pressure, the temperature that export gas to greatest extent.
The present invention increases the temperature difference to strengthen heat absorption capacity, improves heat conduction, improves the thermal efficiency; Make heat transfer intensity even as far as possible, specific heat is even, reduces local frosting, freezing; Utilize the thermodynamic behaviour of compressible fluid, improve heat exchange efficiency, improve and export gas temperature; Utilizing physical method to become steam state when entering, not using extra power, can not allow and provide the liquid of thermal source to freeze, keep the temperature difference; Vacuum generator is gone out and is become ultralow temperature gas, and heat exchange is even; Utilize compressible fluid to improve heat exchange efficiency, allow the gas exported carry heat as much as possible, output temperature high as far as possible.
The present invention may be used for the liquid gasification of various pressure, temperature ,-240 DEG C ~+300 DEG C; Can use when high pressure, super-pressure, ultralow temperature; Thermal source can be air-source, water source, oil sources, burning things which may cause a fire disaster; Other changes the mode of stream tube area, as parallel pipeline; The form of pipeline arrangement has nothing to do, and uses spiral way or round about manner or other mode can.
The present invention utilizes the kinetic energy of fluid to make evaporimeter internal working medium shuttling movement, accelerates heat exchange, makes heat exchange even;
The gas of vaporizing, gasifying utilizing the fluidic architecture of vacuum generator to introduce of the present invention, the temperature different according to thermal source liquid, suction temperature is different, with liquid state can produce after bog mixes that physics is atomized, vaporizes, gasify different-effect, and through heat hybrid switching, make it major part vaporization, such ultralow temperature gas specific heat is less, temperature is lower, contacts evenly with heat exchange tube wall, and the large temperature difference improves heat exchange efficiency;
The pipeline (gas flow pipe) of the present invention's design is from carefully to slightly, although constantly absorb heat, but the volume expansion of flowing, pressure drop can occur, temperature reduces, thus can create the larger temperature difference as far as possible and absorb heat, close up at export pipeline, cross-sectional area reduces (stream pipe attenuates), causes the gas boost gasified of flowing to heat up, make the gas after the gasification of discharging have maximum pressure and temperature, improve heat exchange efficiency.
The present invention utilizes the cold and hot separating effect of the air-flow of vortex tube, makes the output gas temperature after gasifying higher than the temperature of thermal source liquid, can further increase heat exchange efficiency.
When not having gas to flow, be then equivalent to common gasifier, static gas flow pipe change does not have the effect of lifting pressure, lifting temperature; The rotary speed that vortex tube gas forms eddy current is very low, and do not have eddy current to be separated the effect of hot and cold air, in pipeline, liquid gasification process is close or identical with traditional gasifier.
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, within the spirit and principles in the present invention all, any amendment done, equivalent replacement, improvement etc., all should be included within protection scope of the present invention.
Claims (3)
1.
a kind of new liquid intensification gasification installation, is characterized in that, comprising: the outlet of gasifier (1), thermal source liquid (2), gasified liquid entrance (3), thermal source liquid entrance (4) and eddy current high-temperature gas outlet (5); Described thermal source liquid outlet (2) connects gasifier (1); It is outside that described gasified liquid entrance (3) is arranged on gasifier (1); Described thermal source liquid entrance (4) connects gasifier (1); It is outside that described eddy current high-temperature gas outlet (5) is arranged on gasifier (1); Vacuum generator (6), muffler (7), vacuum generator outlet (8), the first connector (9), thin heat exchanger tube (10), the second connector (11), middle heat exchanger tube (12), the 3rd connector (13), thick heat exchanger tube (14), the 4th connector (15), gradient tube (16) and vortex tube (17) is provided with in described gasifier (1); Described gasified liquid entrance (3) connects vacuum generator (6); Described vacuum generator (6) connects vacuum generator outlet (8); Described muffler (7) connects vacuum generator (6); Described vacuum generator outlet (8) connects the first connector (9); Described first connector (9) connects thin heat exchanger tube (10); Described thin heat exchanger tube (10) connects the second connector (11); Heat exchanger tube (12) during described second connector (11) connects; Described middle heat exchanger tube (12) connects the 3rd connector (13); Described 3rd connector (13) connects thick heat exchanger tube (14); Described thick heat exchanger tube (14) connects the 4th connector (15); Described 4th connector (15) connects gradient tube (16); Described gradient tube (16) connects vortex tube (17); Described vortex tube (17) connects the outlet of eddy current high-temperature gas (5) and muffler (7) respectively.
2.
utilize a method of work for new liquid intensification gasification installation as claimed in claim 1, it is characterized in that, comprise the following steps:
s1, described thermal source liquid entrance (4) input thermal source liquid;
s2, is input to vacuum generator (6) liquid to be gasified from gasified liquid entrance (3) with pump;
s3, the morphogenetic jet drive surrounding liquid of liquid that described vacuum generator (6) is to be vaporized or gas flow together, vacuum action is formed, thus by the gas that pipeline suction part has gasified, with jet mixing at muffler (7), gas temperature declines, the heat-transmission of portion gas disengaged vapor makes fluid temperature rise, and a part of liquid heats up and gasifies, different according to the gas temperature sucked from muffler (7), institute's heat content is different, forms atomization, vaporization, gasification result;
s4, exports (8) by vacuum generator export along with jet and muffler (7) suction gas is mixed to form vaporific or vaporous or the gas that is gasified totally in described vacuum generator (6);
s5, the fog-like liquid that described vacuum generator outlet (8) exports or vaporous liquid or gas output to thin heat exchanger tube (10) by the first connector (9);
s6, be in the liquid gas of gaseous state or the lower vaporization of temperature or atomization, enter in thin heat exchanger tube (10) with vaporific or vaporous or gas form, along with outer wall and be full of thermal source liquid institute heat content in gasifier import heat exchange in pipeline into, the inside is still in liquid liquid and comes to life vaporization, the gas heating vaporize, gasified, along with boiling, along with intensification, volumetric expansion, become compressible fluid by the incompressible fluid of liquid state, pressure raises, and temperature is close to the hydrothermal sources providing heat outside tube wall;
s7, the liquid of gasification is after the heat exchanger tube (12) that the second connector (11) enters into cross-sectional area increase, because realizing expanding, pressure drop, temperature declines, in pipeline, gas and pipeline external heat source liquid temperature difference increase, heat absorption capacity increases, and continues to heat up, and pressure progressively gos up, pipeline internal-external temperature difference moves closer to, and trends towards balance heat transfer; Thick heat exchanger tube (14) is entered into again by the 3rd connector (13), heat exchanging pipe area increases again, the gas pressure of gasify in pipeline, vaporizing declines again, temperature declines again, increase with pipeline external heat source liquid temperature difference, heat absorption capacity increases, and continues again heat absorption and heats up, heat absorption boosting, is then outputted to by the 4th connector (15) and connects gradient tube (16);
s8, in time connecting gradient tube (16), pipeline area progressively reduces, pressure progressively increases, temperature rises, and reaches or a little more than the temperature of thermal source liquid, can then enter vortex tube (17), by vortex tube (17) interior air-flow one-to-two again, export higher temperature gas and lower temperature gas respectively; The gas of high temperature is exported by eddy current high-temperature gas outlet (5); Another part comparatively cryogenic gas backs vacuum generator (6) from eddy current cryogenic gas outlet (18) by muffler (7), again mixes in vacuum generator (6);
s9, enters next working cycles.
3.
new liquid intensification gasification installation method of work according to claim 2, it is characterized in that, described step S8 is specially: when treating that gasifying liquid flow is less, the rotary speed that vortex tube gas forms eddy current is very low, do not have eddy current to be separated the effect of hot and cold air, in pipeline, liquid gasification process is close or identical with traditional gasifier.
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| CN104359260B (en) * | 2014-12-09 | 2016-09-07 | 苟仲武 | A kind of evaporimeter potentiating and anti-caking frost device and using method thereof |
| CN104482784B (en) * | 2014-12-16 | 2016-08-24 | 苟仲武 | A kind of efficient liquid intensification gasification installation and method thereof |
| JP6771407B2 (en) * | 2017-03-07 | 2020-10-21 | 株式会社フェザーグラス | Heat removal method and heat removal system |
| CN108088303B (en) * | 2018-01-05 | 2023-10-03 | 河北爱节能源科技有限公司 | Heat exchanger manufactured by adopting zirconium alloy plate, manufacturing process of zirconium alloy plate and cooling method |
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| JPS60202227A (en) * | 1984-03-26 | 1985-10-12 | Mitsubishi Heavy Ind Ltd | Disposing device for waste in ship |
| CN2124375U (en) * | 1992-02-03 | 1992-12-09 | 河北工学院 | Upward and downward gas waste heat centralized recoverer for gasification of coal |
| CN202853431U (en) * | 2012-09-28 | 2013-04-03 | 北京工业大学 | Organic Rankine cycle evaporator used for engine exhaust emission waste heat recovery |
| CN204027387U (en) * | 2014-08-22 | 2014-12-17 | 苟仲武 | A kind of new liquid intensification gasification installation |
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| US20120152399A1 (en) * | 2010-12-20 | 2012-06-21 | Marc Gregory Allinson | F.U.N tunnel(s) |
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Patent Citations (4)
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|---|---|---|---|---|
| JPS60202227A (en) * | 1984-03-26 | 1985-10-12 | Mitsubishi Heavy Ind Ltd | Disposing device for waste in ship |
| CN2124375U (en) * | 1992-02-03 | 1992-12-09 | 河北工学院 | Upward and downward gas waste heat centralized recoverer for gasification of coal |
| CN202853431U (en) * | 2012-09-28 | 2013-04-03 | 北京工业大学 | Organic Rankine cycle evaporator used for engine exhaust emission waste heat recovery |
| CN204027387U (en) * | 2014-08-22 | 2014-12-17 | 苟仲武 | A kind of new liquid intensification gasification installation |
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