CN105403066A - Condenser - Google Patents
Condenser Download PDFInfo
- Publication number
- CN105403066A CN105403066A CN201510984373.1A CN201510984373A CN105403066A CN 105403066 A CN105403066 A CN 105403066A CN 201510984373 A CN201510984373 A CN 201510984373A CN 105403066 A CN105403066 A CN 105403066A
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- liquid
- liquid refrigerant
- working medium
- cavity
- condenser
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B3/00—Condensers in which the steam or vapour comes into direct contact with the cooling medium
- F28B3/06—Condensers in which the steam or vapour comes into direct contact with the cooling medium by injecting the steam or vapour into the cooling liquid
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A condenser comprises a condenser body, wherein at least one air inlet and at least one liquid outlet are formed in the condenser body; at least one empty chamber which communicates with the at least one air inlet and the at least one liquid outlet is formed in the condenser body; a liquid working medium is stored in the empty chamber which communicates with the at least one air inlet and the at least one liquid outlet; a gaseous working medium is in contact with the liquid working medium in the empty chamber through the air inlet; the liquid working medium in the empty chamber runs through the liquid outlet; the liquid working medium in the empty chamber comprises all substances which are included in the contacted gaseous working medium; the temperature of the liquid working medium in the empty chamber is lower than that of the contacted gaseous working medium. The condenser has the advantage of being high in heat exchange efficiency; the condenser is mainly applied to a steam engine and can replace the condenser in the steam engine.
Description
Technical field
The present invention relates to a kind of device of gas liquefaction, be mainly used in steam engine, replace condenser wherein.
Background technology
Condenser is the parts of refrigeration system, belong to the one of heat exchanger, gas can be become liquid, condenser working process is an exothermic process, power plant is that the steam that turbine is discharged obtains condensation with many condensers, carrys out the refrigerant vapor of condensation ammonia and freon and so at refrigeration plant's condenser.Petro chemical industry condenser makes hydro carbons and other chemical evapn condensations, condenser liberated heat is latent heat, the general name of latent heat latent heat of phase change, object when isothermal and isobaric, absorb or liberated heat from a phase change to another phase, it is the heat of condensation that gas becomes liquid, and what condenser was released is the heat of condensation.Condenser is gas by a long pipe by heat loss in the air of surrounding, and therefore condenser has air inlet and liquid outlet, but the speed of the existing condenser liquid gas shortcoming that namely heat exchange efficiency is low slowly.
Summary of the invention
The present invention aims to provide the high condenser of a kind of heat exchange efficiency.
To achieve these goals, the principles of science of a kind of condenser of the present invention is that the present invention proposes first, conveniently describe, gaseous working medium is set to A gas, liquid after A gas liquefaction is A liquid, the liquid that the liquid dissolved each other with A liquid arbitrary proportion forms is set to B liquid, B liquid can be the mixing material of one or more liquids composition, A gas is a kind of gaseous material, the temperature of A gas is higher than the temperature of the liquid contacted with A gas, when A gas and A liquid, or with B liquid, or when contacting with the mixing material that A liquid and B liquid form, unlimited ratio is dissolved in contacted liquid by A gas, and release heat to it, the fluid temperature contacted rises, the liquid that A gas contacts is called liquid refrigerant, A gas is called gaseous working medium, because the unlimited ratio of A gas is dissolved in the liquid refrigerant of its contact, so A liquid must be comprised in liquid refrigerant.
The invention discloses a kind of condenser, comprise body, described body is provided with at least one air inlet and at least one liquid outlet, the cavity that at least one communicates with at least one air inlet described and at least one liquid outlet described is provided with in described body, liquid refrigerant in the cavity that at least one air inlet described and described and at least one liquid outlet described communicate, gaseous working medium is by described air inlet and contact with the liquid refrigerant in described cavity, liquid refrigerant in described cavity is by described liquid outlet, liquid refrigerant in described cavity comprises all kinds of materials that the gaseous working medium that contacts with the liquid refrigerant in described cavity comprises, the temperature of the liquid refrigerant in described cavity is lower than the temperature of the gaseous working medium contacted with the liquid refrigerant in described cavity.
Further, a kind of condenser of the present invention, often kind of liquid arbitrary proportion in the liquid refrigerant in described cavity dissolves each other the liquid of at least one gaseous material post liquefaction in the gaseous working medium contacted with the liquid refrigerant in described cavity.
Further, a kind of condenser of the present invention, often kind of liquid arbitrary proportion in the liquid refrigerant in described cavity dissolves each other the liquid of in the gaseous working medium contacted with the liquid refrigerant in described cavity each gaseous material post liquefaction.
Further, a kind of condenser of the present invention, the interior thereof of the liquid refrigerant in described gaseous working medium and described cavity touches, and further, a kind of condenser of the present invention, described condenser also comprises the solid matter that the liquid refrigerant in described cavity dissolves.
Gaseous working medium in foregoing is that the gaseous material contacted with described liquid refrigerant forms, described gaseous working medium is at least one gaseous material, in foregoing, material representative is meant to simple substance or compound, material be meant to a kind of compound or an a kind of simple substance, the liquid refrigerant in foregoing is made up of at least one liquid.
Beneficial effect of the present invention: liquid gas speed is fast, and the present invention by adding liquid refrigerant, thus changes the performance of condenser on the whole, improves heat exchange efficiency.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the body with vertical radiating tube.
Fig. 2 is the schematic diagram that gas divides guide hole plate.
Fig. 3 is the schematic diagram of the body with heatsink transverse pipe.
Fig. 4 is the schematic diagram of the body with two air inlets and a liquid outlet and an inlet.
Fig. 5 is the schematic diagram of the body with an air inlet and two liquid outlets and an inlet.
Fig. 6 is the schematic diagram in body with two cavitys.
Fig. 7 is the general illustration that the present invention is applied to steam engine.
Fig. 8 is the direction view of irregular shape mouth.
Fig. 9 is the direction view of annular mouth.
Figure 10 is the direction view of rectangle hole.
Figure 11 is the direction view of circular port.
Figure 12 is the schematic diagram of the body with an air inlet and a liquid outlet, see in Fig. 1-12, 1-visor, 2-check valve, 3-liquid outlet, 4-air inlet, 5-gas divides guide hole plate, the vertical radiating tube of 6-, 7-cavity, 8-body, 9-check valve, 10-air inlet, 11-top catch box, 12-heatsink transverse pipe, 13-body, 14-cavity, 15-bottom catch box, 16-gas divides guide hole plate, 17-liquid outlet, 18-air inlet, 19-body, 20-cavity, 21-liquid outlet, 22-inlet, 23-air inlet, 24-air inlet, 25-body, 26-cavity, 27-liquid outlet, 28-inlet, 29-liquid outlet, 47-electric centrifugal pump, 52-breather check valve, 30-liquid outlet, 31-liquid outlet, 32-liquid outlet, 33-inlet, 34-air inlet, 35-air inlet, 36-inlet, 37-liquid outlet, 38-cavity, 39-cavity, 40-body, 46-electric centrifugal pump, 48-electric centrifugal pump, 50-breather check valve, 51-breather check valve, the air inlet of a 41-condenser, the liquid outlet of a 42-condenser, 43-evaporimeter, 44-mechanical energy converter, 45-condenser, 49-reflux pump, 56-liquid outlet, 53-air inlet, 54-body, 55-cavity.
Detailed description of the invention
Embodiment one, as Fig. 1, body 8 comprises check valve 2 and visor 1 and vertical radiating tube 6 and gas and divides guide hole plate 5 and air inlet 4 and liquid outlet 3, a cavity 7 is provided with in body 8, cavity 7 built with liquid refrigerant be water, gaseous working medium is steam, water injects in cavity 7 from check valve 2, till visor 1 sees liquid level, steam obtains by heating boiler, make the temperature of steam higher than the temperature of liquid refrigerant water, steam enters in cavity 7 from air inlet 4, guide hole plate 5 is divided to be divided into tiny bubble by gas, touch with the interior thereof of the liquid refrigerant in cavity, gas divides the concrete structure of guide hole plate 5 as Fig. 2, increase the contact area with water, increase the solute effect to steam, steam mixes with water after dissolving, outwards dispelled the heat by vertical radiating tube 6, many liquid refrigerant water is discharged from liquid outlet 3, liquid outlet 3 communicates with air, make liquid refrigerant water lower than its boiling point.The A direction view of liquid outlet 3 is Figure 11 liquid outlet is circle, and B direction view such as the shape of Figure 10 air inlet of air inlet 4 is rectangle, dissolves some solid NuaO in described liquid refrigerant, to reduce the freezing point of liquid refrigerant.
Embodiment two, as Fig. 3, body 13 comprises check valve 9 and top catch box 11 and liquid outlet 17 and heatsink transverse pipe 12 and bottom catch box 15 and gas and divides guide hole plate 16, with air inlet 10, a cavity 14 is provided with in body 13, cavity 14 is the mixing material that water and ethanol form built with liquid refrigerant, gaseous working medium is alcohol vapor, liquid refrigerant injects in cavity 14 from check valve 9, until cavity 14 fills, alcohol vapor can be obtained by heating boiler, make the temperature of temperature higher than liquid refrigerant of gaseous working medium, alcohol vapor enters in cavity 14 from air inlet 10, contact with liquid refrigerant, guide hole plate 16 is divided by the gas of bottom catch box 15, be divided into minute bubbles, touch with the interior thereof of liquid refrigerant, with enlarge active surface, mix with liquid refrigerant after dissolving, gas divides the concrete structure of guide hole plate 16 as Fig. 2, top catch box 11 is arrived by heatsink transverse pipe 12, many liquid refrigerants are discharged from liquid outlet 17, liquid outlet 17 communicates with air, externally dispelled the heat by body 13, make the temperature of liquid refrigerant lower than its boiling point, the D direction view of air inlet 10 to be the shape of Fig. 9 air inlet be annular, the C direction view of liquid outlet 17 to be the shape of Fig. 9 liquid outlet be annular, some solid sodium chlorides are dissolved in described liquid refrigerant, to reduce the freezing point of liquid refrigerant.
Embodiment three, as Fig. 4, a cavity 20 is provided with in body 19, gaseous working medium is the gas that alcohol vapor and methanol vapor mix, liquid refrigerant is the mixing material of methyl alcohol and ethanol composition, alcohol vapor and methanol vapor can be obtained by heating two boilers, make the temperature of temperature higher than liquid refrigerant of gaseous working medium, liquid refrigerant is filled in cavity 20, gaseous working medium enters in cavity 20 by air inlet 23 and air inlet 18, contact with the liquid refrigerant in cavity, mix with liquid refrigerant after dissolving, also has electric centrifugal pump 47, liquid outlet 21 is connected with the inlet of cooler, cooler is provided with liquid outlet and communicates with air, liquid refrigerant is provided with from described cooler the liquid outlet communicated with air and discharges, cooler is also provided with liquid outlet to be connected with inlet 22, the temperature of liquid refrigerant is reduced by cooler, make liquid refrigerant lower than its boiling point, the F direction view of liquid outlet 21 is Figure 11, the shape of liquid outlet is circular, the inlet shape of inlet 22 is also circular, the E direction view of air inlet 23 is the shape of Fig. 8 air inlet is irregular, air inlet 18 is identical with the intake port shape of air inlet 23.
Embodiment four, as Fig. 5, gaseous working medium is the gas that methanol vapor and alcohol vapor mix, liquid refrigerant is the liquid that methyl alcohol and second alcohol and water mix, in the cavity 26 be provided with in liquid refrigerant injector body 25, till filling, gaseous working medium can be obtained by heating boiler, make the temperature of temperature higher than liquid refrigerant of gaseous working medium, gaseous working medium enters cavity 26 from air inlet 24, and contact with interior liquid refrigerant, the effect of breather check valve 52 prevents liquid refrigerant from flowing out from air inlet, many liquid refrigerants are discharged from liquid outlet 29, liquid outlet 29 communicates with air, liquid outlet 27 is connected with the liquid feeding end of cooler, inlet 28 is connected with the outlet end of described cooler, the temperature of liquid refrigerant is reduced by cooler, make liquid refrigerant lower than its boiling point.
Embodiment five, as Fig. 7, apply the present invention in steam engine, replace the condenser in steam engine, wherein gaseous working medium is R12 steam, liquid refrigerant is liquid R12, first liquid refrigerant is injected a kind of condenser 45, liquid R12 in evaporimeter 43 is heated vaporization, produce the gas of high pressure, the gas of high pressure enters in mechanical energy converter 44 by pipeline, mechanical energy converter 44 is in the form of piston, promotion piston does work, the gaseous working medium of discharging enters a kind of air inlet 41 of condenser by pipeline thus contacts with the liquid refrigerant in a kind of condenser 45, enter a kind of temperature of gaseous working medium of condenser 45 higher than the temperature with the liquid refrigerant in described a kind of condenser 45, many liquid refrigerants are discharged from a kind of liquid outlet 42 of condenser, enter in reflux pump 49 through piping, reflux pump 49 is plunger type, liquid refrigerant pushes back in evaporimeter 43 by reflux pump 49, complete a working cycles thus, gaseous working medium and liquid refrigerant also can be R22.
Embodiment six, as Fig. 6, two cavitys are provided with in body 40, cavity 38 and cavity 39, the gaseous working medium entered in cavity 38 is methanol vapor, liquid refrigerant in cavity 38 is the liquid that methyl alcohol and water form, the temperature of the liquid refrigerant in cavity 38 is lower than the temperature of the gaseous working medium in cavity 38, methanol vapor can be obtained by heating boiler, methanol vapor enters in cavity 38 by air inlet 35, many liquid refrigerants are discharged from liquid outlet 30, liquid outlet 30 communicates with air, the temperature reducing the liquid refrigerant in cavity 38 makes it lower than its boiling point, also has electric centrifugal pump 46, liquid outlet 37 is communicated with a cooler with inlet 36, the gaseous working medium entered in cavity 39 is alcohol vapor, alcohol vapor can be obtained by heating boiler, liquid refrigerant in cavity 39 is the liquid of ethanol and cyclohexane composition, the temperature of the alcohol vapor in described cavity 39 is higher than the temperature of the liquid refrigerant in cavity 39, alcohol vapor enters liquid refrigerants many in cavity 39 by air inlet 34 and is discharged by liquid outlet 31, also has electric centrifugal pump 48, liquid outlet 32 is connected with another cooler with inlet 33, liquid outlet 31 communicates with air, the temperature reducing the liquid refrigerant in cavity 39 makes it lower than its boiling point, breather check valve 50 and breather check valve 51 flow out from air inlet for preventing liquid refrigerant.
Embodiment seven, as Fig. 6, two cavitys are provided with in body 40, cavity 38 and cavity 39, gaseous working medium is all steam, steam can be obtained by heating boiler, liquid refrigerant in cavity 38 and cavity 39 is all the liquid that water and ethanol are mixed into, in each cavity, the temperature of gaseous working medium is higher than the temperature of liquid refrigerant, steam enters in cavity 38 and cavity 39 by air inlet 35 and air inlet 34, touch with the interior thereof of liquid refrigerant, liquid outlet 37 is connected with a cooler with inlet 36, liquid outlet 32 is connected with another cooler with inlet 33, breather check valve 50 and breather check valve 51 flow out from air inlet for preventing liquid refrigerant, many liquid refrigerants are discharged from liquid outlet 30 and liquid outlet 31, liquid outlet 31 communicates with air, the temperature reducing the liquid refrigerant in cavity 39 makes it lower than its boiling point, liquid outlet 30 communicates with air, the temperature reducing the liquid refrigerant in cavity 38 makes it lower than its boiling point, also have electric centrifugal pump 46 and electric centrifugal pump 48.
Embodiment eight, as Fig. 1, gaseous working medium is the gas that steam mixes with ether fume, liquid refrigerant is the liquid that water and dimethyl sulfoxide (DMSO) and ether and cyclohexane are mixed into, in cavity 7, liquid refrigerant is injected by check valve 2, till visor 1 sees liquid level, gaseous working medium enters in cavity 7 from air inlet 4, steam and ether fume can be obtained by heating boiler, the temperature of gaseous working medium is higher than the temperature of liquid refrigerant, many liquid refrigerants are discharged from liquid outlet 3, vertical radiating tube 6 externally dispels the heat, liquid outlet 3 communicates with air, make the temperature of liquid refrigerant lower than its boiling point.
Embodiment nine, as Fig. 1, gaseous working medium is the gas that cyclohexane vapor and steam mix, and liquid refrigerant is the liquid that cyclohexane and water mix, and fills liquid refrigerant in cavity 7, gaseous working medium is entered in cavity by air inlet 4 and touches with the interior thereof of liquid refrigerant, gaseous working medium can be obtained by heating boiler, and the temperature of gaseous working medium is higher than the temperature of liquid refrigerant, and many liquid refrigerants are discharged from liquid outlet 3, liquid outlet 3 communicates with air, keeps the temperature of liquid refrigerant lower than its boiling point.
Embodiment ten, as Fig. 1, gaseous working medium is the gas that n-hexane steam and steam are mixed into, liquid refrigerant is the liquid that n-hexane and water mix, gaseous working medium can be obtained by heating boiler, make the temperature of temperature higher than liquid refrigerant of gaseous working medium, liquid refrigerant fills cavity 7, gaseous working medium is entered in cavity 7 by air inlet 4 and contacts with liquid refrigerant, guide hole plate 5 is divided to be divided into tiny bubble by gas, many liquid refrigerants are discharged by liquid outlet 3, and liquid outlet 3 communicates with air, keep liquid refrigerant lower than its boiling point.
Embodiment 11, as Figure 12, body 54 comprises an air inlet 53 and a liquid outlet 56, a cavity 55 is provided with in body 54, gaseous working medium can be obtained by heating boiler, the temperature of gaseous working medium is higher than the temperature of liquid refrigerant, gaseous working medium enters cavity 55 from air inlet 53, liquid refrigerant is arranged in cavity 55, and fill cavity 55, body 54 externally dispels the heat, keep the temperature of liquid refrigerant lower than its boiling point, many liquid refrigerants are discharged from liquid outlet 56, liquid outlet 56 communicates with air, gaseous working medium is steam liquid refrigerant is that water and cyclohexane mix, or gaseous working medium is that to mix liquid refrigerant be the liquid that methyl alcohol and second alcohol and water mix for methanol vapor and alcohol vapor, or gaseous working medium is the liquid that steam and ether fume form that liquid refrigerant is water and dimethyl sulfoxide (DMSO) and ether and cyclohexane composition.
Embodiment 12, as Figure 12 changes liquid outlet 56 into air inlet, change air inlet 53 into liquid outlet, liquid refrigerant is the liquid of water and methyl alcohol and ethanol composition, gaseous working medium is the gas of steam and methanol vapor and alcohol vapor composition, gaseous working medium can be obtained by heating boiler, the temperature of gaseous working medium is higher than the temperature of the liquid refrigerant in cavity 55, gaseous working medium enters in cavity 55 from air inlet 56 and contacts with liquid refrigerant, many liquid refrigerants are discharged from liquid outlet 53, liquid outlet 53 communicates with air, externally dispelled the heat by body 54, keep the temperature of liquid refrigerant lower than its boiling point.
Gaseous working medium in the present invention and liquid refrigerant are not limited to the material in above embodiment, other material can also be comprised, the effect circulating fluid of electric centrifugal pump, liquid refrigerant is more evenly contacted with gaseous working medium, more be conducive to heat radiation, above embodiment can add electric centrifugal pump, described although the present invention passes through as above preferred embodiment, but a variety of distortion can also be had according to technical scheme of the present invention, do not departing from the change made under the prerequisite of Spirit Essence of the present invention and distortion and all should belong to the protection domain of appended claim of the present invention.
Claims (5)
1. a condenser, comprise body, described body is provided with at least one air inlet and at least one liquid outlet, it is characterized in that, the cavity that at least one communicates with at least one air inlet described and at least one liquid outlet described is provided with in described body, liquid refrigerant in the described cavity communicated with at least one air inlet described and at least one liquid outlet described, gaseous working medium is by described air inlet and contact with the liquid refrigerant in described cavity, liquid refrigerant in described cavity is by described liquid outlet, liquid refrigerant in described cavity comprises all kinds of materials that the gaseous working medium that contacts with the liquid refrigerant in described cavity comprises, the temperature of the liquid refrigerant in described cavity is lower than the temperature of the gaseous working medium contacted with the liquid refrigerant in described cavity.
2. condenser according to claim 1, the often kind of liquid arbitrary proportion that it is characterized in that in the liquid refrigerant in described cavity dissolves each other the liquid of at least one gaseous material post liquefaction in the gaseous working medium contacted with the liquid refrigerant in described cavity.
3. condenser according to claim 1 and 2, the often kind of liquid arbitrary proportion that it is characterized in that in the liquid refrigerant in described cavity dissolves each other the liquid of in the gaseous working medium contacted with the liquid refrigerant in described cavity each gaseous material post liquefaction.
4., according to the condenser described in claim 3, it is characterized in that the interior thereof of the liquid refrigerant in described gaseous working medium and described cavity touches.
5., according to the condenser described in claim 3, it is characterized in that described condenser also comprises the solid matter of the liquid refrigerant dissolving in described cavity.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510984373.1A CN105403066A (en) | 2015-08-19 | 2015-12-25 | Condenser |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510507077 | 2015-08-19 | ||
| CN2015105070772 | 2015-08-19 | ||
| CN201510984373.1A CN105403066A (en) | 2015-08-19 | 2015-12-25 | Condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105403066A true CN105403066A (en) | 2016-03-16 |
Family
ID=55468708
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510984373.1A Pending CN105403066A (en) | 2015-08-19 | 2015-12-25 | Condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105403066A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106595332A (en) * | 2016-12-16 | 2017-04-26 | 于小峰 | Condenser |
| CN111994985A (en) * | 2020-08-25 | 2020-11-27 | 孔令斌 | Solar seawater desalination device with water storage and condensation functions |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87100862A (en) * | 1986-01-08 | 1987-09-30 | 奥马蒂系统公司 | The working fluid that is used for rankine cycle power plant |
| CN1275707A (en) * | 1999-05-31 | 2000-12-06 | 上原春男 | Absorption device |
| CN104728061A (en) * | 2015-03-27 | 2015-06-24 | 重庆天豪建材有限责任公司 | Low-temperate geothermal power generation system |
-
2015
- 2015-12-25 CN CN201510984373.1A patent/CN105403066A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87100862A (en) * | 1986-01-08 | 1987-09-30 | 奥马蒂系统公司 | The working fluid that is used for rankine cycle power plant |
| CN1275707A (en) * | 1999-05-31 | 2000-12-06 | 上原春男 | Absorption device |
| CN104728061A (en) * | 2015-03-27 | 2015-06-24 | 重庆天豪建材有限责任公司 | Low-temperate geothermal power generation system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106595332A (en) * | 2016-12-16 | 2017-04-26 | 于小峰 | Condenser |
| CN111994985A (en) * | 2020-08-25 | 2020-11-27 | 孔令斌 | Solar seawater desalination device with water storage and condensation functions |
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