CN106969549B - Marine flowing type evaporator and application method thereof - Google Patents
Marine flowing type evaporator and application method thereof Download PDFInfo
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- CN106969549B CN106969549B CN201710324596.4A CN201710324596A CN106969549B CN 106969549 B CN106969549 B CN 106969549B CN 201710324596 A CN201710324596 A CN 201710324596A CN 106969549 B CN106969549 B CN 106969549B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/02—Evaporators
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/04—Arrangements for sealing elements into header boxes or end plates
- F28F9/16—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling
- F28F9/18—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling by welding
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/24—Arrangements for promoting turbulent flow of heat-exchange media, e.g. by plates
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Fluid Mechanics (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention relates to a marine flowing type evaporator, which comprises a cylinder body, a heat exchange tube bundle, an air outlet pipe and a liquid inlet, wherein the cylinder body is provided with a liquid inlet; a group of baffle plates are fixed on the inner wall of the cylinder body in the direction perpendicular to the inner wall of the cylinder body, small holes for the heat exchange tube bundles to pass through are formed in the baffle plates, and the baffle plates divide the inside of the cylinder body into refrigerant channels for the refrigerant to wash the heat exchange tube bundles back and forth; the air outlet pipe is vertically upwards, and the liquid inlet pipe can be arranged at any corresponding position on the cylinder body according to the arrangement of the refrigerant channels; the flow direction of the non-refrigerant liquid in the heat exchange tube bundle is opposite to the flow direction of the refrigerant in the cylinder. The invention has the advantages of a dry evaporator, a flooded evaporator and a falling film evaporator, overcomes the defects of the dry evaporator, the flooded evaporator and the falling film evaporator, and has the characteristics of compact structure, convenient oil return, low refrigerant flushing quantity, high heat exchange coefficient, high degree of freedom of liquid inlet arrangement and the like.
Description
Technical Field
The invention relates to a marine flowing type evaporator and a use method thereof, belonging to the technical field of refrigeration.
Background
The existing shell-and-tube evaporator comprises a dry evaporator, a flooded evaporator and a falling film evaporator. The dry evaporator has low heat exchange coefficient, the heat exchange tube adopts an internal thread copper tube, water flows outside the tube, the tube wall is washed by the action of a baffle plate, heat exchange is improved, the refrigerant flows in the tube, oil flows out of the evaporator along with the refrigerant, so that the reliability is higher, in addition, the refrigerant filling amount is smaller, and the dry evaporator is suitable for jolt occasion where a ship is located, and has the defect of poor heat exchange effect.
The full-liquid evaporator has high heat exchange coefficient, the inside of the heat exchange tube adopts internal thread to strengthen flow, the outer surface adopts evaporation strengthening design, belongs to pool boiling, has good heat exchange effect, is largely used in a central air conditioner host, is currently a full-liquid evaporator on the market, adopts bottom middle liquid inlet, uniformly distributes gas-liquid two phases into an evaporation tube bundle through a bottom distributor, uniformly distributes gas-liquid into the whole container, ensures that the temperature of liquid refrigerant is uniform, ensures that the evaporation temperature is uniform, ensures that the distribution of oil concentration is uniform, reduces the oil return effect of a unit, leads to higher oil concentration in the evaporator, leads to oil loss of a compressor and leads to low oil level alarm of the compressor; secondly, oil enters the reinforced pores outside the pipe, and the evaporation reinforcing effect is affected; in the aspect of design of air outlet, the common practice is to place a baffle plate with the width about 10 times of the air suction pipe diameter at the position of about twice of the air suction pipe diameter below the air outlet, so as to prevent the air suction from directly taking away the liquid refrigerant below the air suction port. However, this solution still causes a lot of liquid refrigerant to fly, since the air flow rate at the inlet of the baffle still reaches 2 m/s, and in order to reduce the air flow rate, only the height of the baffle can be reduced, firstly the evaporator space is reduced, and secondly the baffle is close to the pool surface, and still liquid refrigerant is easily carried away; in terms of refrigerant charge, the flooded charge is greatest. Because the ship can shake, the liquid of the flooded evaporator can be easily shaken out in the running process, and the existing land flooded evaporator is not suitable for being used in the ship occasion.
The falling film evaporator has high heat exchange coefficient, the inside of the heat exchange tube adopts internal thread reinforced flow, the outer surface adopts evaporation reinforced design, the refrigerant is distributed by a distributor at the top, the liquid uniformly falls onto the horizontally arranged heat exchange tubes, the gravity impact effect improves the heat exchange effect, the oil is concentrated along with the falling and evaporation of the refrigerant, the concentration reaches the bottom of the heat exchanger to the maximum, the oil return can be carried out by adopting a simple method, and the reliability of the unit is high; in the aspect of refrigerant filling, the filling amount of the falling film evaporator is equal to 70% of the filling amount. Similarly, the ship can shake, and the liquid of the full-liquid evaporator can be easily shaken out in the running process, so that the existing land full-liquid evaporator is not suitable for being used in ship occasions.
Disclosure of Invention
The technical problems to be solved by the invention are as follows: the existing marine flooded evaporator is poor in oil return effect, low in evaporator exchange efficiency, high in refrigerant flushing and injection quantity, and insufficient in reliability, because the ship jolts, liquid refrigerant in the heat exchanger is prevented from shaking and then is discharged from the air outlet pipe to cause liquid impact risks to the compressor, the heat exchanger is also forced to be large in size, more installation space is occupied, and the reliability is also insufficient.
The invention adopts the following technical scheme:
a marine mobile evaporator comprises a cylinder 2, a heat exchange tube bundle 3, an air outlet tube 6 and a liquid inlet 5; a group of baffle plates 8 are fixed on the inner wall of the cylinder 2 in the direction perpendicular to the inner wall of the cylinder, small holes for the heat exchange tube bundles 3 to pass through are formed in the baffle plates 8, and the baffle plates 8 divide the inside of the cylinder into refrigerant channels for the refrigerant to wash the heat exchange tube bundles 3 back and forth; the air outlet pipe 6 is vertically upwards, and the liquid inlet pipe 5 can be arranged at any corresponding position on the cylinder 2 according to the arrangement of the refrigerant channels; the flow direction of the non-refrigerant liquid in the heat exchange tube bundle 3 is opposite to the flow direction of the refrigerant in the cylinder 2.
Further, the baffle plate 8 is semicircular, and the marine flow type evaporator is of a single-flow structure.
Further, the device also comprises a separation plate 4, wherein the separation plate 4 separates the cylinder 2 into at least two equal parts, each equal part forms a refrigerant flow passage, and a fan-shaped baffle plate 8 covers a part of the sectional area of the refrigerant flow passage; one end of the partition plate 4 is fixedly connected with the end plate 1, the other end of the partition plate is provided with a notch, and the notch is the communicating part of two adjacent flow channels.
Furthermore, the partition plate 4 is a flat plate penetrating through the central axis of the cylinder body to divide the cylinder body into two refrigerant flow channels, the baffle plate 8 is in a 90-degree fan shape, and the refrigerant flow channels with semicircular cross sections are divided into two parts.
Further, the cylinder body 1 is horizontally arranged; the air outlet pipe 6 is close to the water inlet and is vertically arranged at the upper part of the cylinder body 1; the liquid inlet is close to the water outlet.
Furthermore, the heat exchange tube bundle 3 and the end plate 1 are fixed by expansion or welding, the partition plate 4 is attached to the end plate 1 at one end and has no gap, a certain gap is reserved between the other end and the end plate 1, so that the refrigerant can flow from the upper area to the lower area, the partition plate 4 partitions the evaporation tube bundle, the first evaporation area 301 and the second evaporation area 302, the partition number is the same as the flow number of water, and the refrigerant and the water flow in the opposite direction.
Further, the heat exchange tube bundle 3 is partitioned by a partition plate 4 in the height direction or the width direction; the gap between the other end of the partition plate 4 and the end plate 1 increases as the number of refrigerant flows increases; the interval of the baffle plates 8 becomes larger and larger in the refrigerant flow direction.
In the method for using the above-mentioned flow evaporator, when the mixture of two-phase low-pressure low-temperature refrigerant and oil is fed through the liquid inlet 5, the refrigerant can only flow forward in the partition of the heat exchange tube bundle 3 separated by the partition plate 4, and during the flowing process, the refrigerant is subjected to the action of the baffle plate to wash the heat exchange tube bundle 3, and at the end of the partition, the refrigerant enters the next partition through the gap between the other end of the partition plate 4 and the end plate, and then enters the next partition until reaching the air outlet after the same flow is carried out in the next partition; the partition plate 4 partitions the heat exchange tube bundle 3, wherein the number of the partitions is equal to the number of the flow paths of water and the number of the flow paths of refrigerant; the flow direction of water is opposite to the flow direction of the refrigerant, so that countercurrent heat exchange is formed; the air outlet 6 of the refrigerant is close to the water inlet, so that the air outlet can have a certain degree of superheat, and meanwhile, the oil is fully concentrated; the oil flows with the refrigerant and is eventually carried out of the system by the gaseous refrigerant.
In the method for using the above-mentioned flow-type evaporator, a plurality of flow-type evaporators are combined, the outlet of the former flow-type evaporator is the inlet of the next flow-type evaporator, and the combined body comprises a refrigerant liquid inlet 5 and a gas outlet 6, and the relative positions of the two flow-type evaporators are horizontally juxtaposed or vertically stacked.
The use method of the flow type evaporator comprises the steps that the flow type evaporator and the flooded evaporator are combined, the refrigerant flows through the flooded evaporator, gas rises to enter the compressor, and the rest liquid enters the flow type evaporator, is gasified and enters the compressor; alternatively, the combination of a flow evaporator and a falling film evaporator is performed, the refrigerant first flows through the falling film evaporator, the gas rises into the compressor, the remaining liquid enters the flow evaporator, and then is vaporized into the compressor.
The invention has the beneficial effects that: compared with a dry evaporator, the evaporator has the advantages of compact structure, convenient oil return and low refrigerant filling quantity, and has no defect of low heat exchange coefficient; compared with a flooded evaporator, the refrigerant flushing device has the advantages that the refrigerant flushing effect is achieved, the heat exchange coefficient is higher, the heat exchange coefficient is enhanced by 10%, the structure is more compact, the refrigerant filling amount is only 30% (because the density of a gas-liquid mixture is small), and no oil return concerns exist; compared with a falling film evaporator, the falling film evaporator has the same heat exchange coefficient, the structure is more compact, the refrigerant filling amount is lower, and the design cost and the manufacturing cost are lower; the position of the liquid inlet can be freely set according to the flow design, but not necessarily at the bottom of the cylinder, and the freedom degree of structural setting is higher.
The following reasons for the beneficial effects are specifically described:
the structure is compact: because the refrigerant does not have gas-liquid layering in the cylinder, the liquid refrigerant does not need to flow out from the liquid outlet after shaking, and therefore, the upper part of the cylinder does not need to reserve a space for storing the gaseous refrigerant, and the structure can also achieve a compact effect;
the oil return is convenient: the gaseous and liquid refrigerants flow in the cylinder together and carry the frozen oil, so that the frozen oil is prevented from being retained in the cylinder, and the oil return is ensured;
the refrigerant flushing amount is low: the refrigerant is in a gas-liquid mixed flowing state, and the density is lower, so that the flushing quantity of the refrigerant can be lower;
the heat exchange coefficient is high: the refrigerant in the gas-liquid mixing state is used for flushing the evaporation tube bundles back and forth under the action of the baffle plate, so that the heat exchange coefficient is high;
the degree of freedom of the structural arrangement is higher: the liquid inlet of the traditional flooded heat exchanger is required to be arranged at the bottom of the cylinder, so that the distance between the liquid inlet and the air outlet is increased, the problem of reliability caused by splashing of the liquid refrigerant out of the air outlet after shaking is avoided, and the refrigerant in the gas-liquid mixing state flows in the cylinder according to the flow, so that the necessity of arranging the liquid inlet at the bottom of the cylinder is avoided, and the degree of freedom of structural arrangement is higher.
Drawings
Fig. 1, a left side view of a marine flow evaporator heat exchanger of the invention.
FIG. 2, front view of a marine flow evaporator heat exchanger of the invention
Fig. 3, refrigerant single zone flow diagram.
FIG. 4, refrigerant flow diagram in heat exchanger
Fig. 5, schematic view of a 90 sector of baffles.
Fig. 6, water chamber and water flow diagram.
Fig. 7, a left side view of a combination of two flow evaporators.
Fig. 8, a front view of a combination of two flow evaporators.
Fig. 9, a refrigerant flow diagram of a two flow evaporator combination.
Fig. 10, schematic view of a 180 sector baffle.
The legend designations in the drawings indicate the following meanings:
1. the heat exchange tube comprises an end plate, a cylinder body, a heat exchange tube bundle, a partition plate, a liquid inlet and an air outlet, wherein the end plate is provided with the cylinder body;
7A left water chamber, 7B right water chamber, 8. Baffle plate (90 DEG fan), 9. Connecting pipe, 1A left end plate, 1B right end plate, 1U upper end plate, 1D lower end plate, 1UA left upper end plate, 1UB right upper end plate, 1DA left lower end plate, 1DB right lower end plate, 2U upper cylinder, 2D lower cylinder, 3U upper heat exchange tube bundle, 3D lower heat exchange tube bundle, 101. Hanging hole, 102. Bolt hole, 702. Water inlet tank, 703. Water inlet pipe, 704. Water outlet pipe, 705. Water outlet tank, 8S baffle plate (180 DEG fan).
Detailed Description
The invention will be further described with reference to the drawings and specific examples.
The invention relates to a flow type evaporator, which adopts the principle that a dry type evaporator structure is adopted in a shell, a water flow scheme and a refrigerant flow scheme of the evaporator are adopted, so that water flows in a heat exchange tube, the refrigerant flows outside the heat exchange tube, a baffle plate is used for baffling, a liquid refrigerant is driven by a gaseous refrigerant to wash the heat exchange tube, the heat exchange coefficient is improved, a refrigerant inlet is close to a water outlet, a refrigerant outlet is close to a water inlet, oil is carried out of the evaporator along with the flow of the gaseous refrigerant, a heat exchange tube bundle is partitioned by a partition plate, the partition number is the same as the flow number of the water flow, and the flow of the refrigerant and the flow of the water are reversed, so that countercurrent heat exchange is formed.
Embodiment one:
the embodiment is a flow evaporator used in a refrigeration air conditioning system with refrigeration capacity of 500kW, chilled water backwater temperature of 12 ℃, water outlet temperature of 7 ℃, evaporation temperature of 6.5 ℃ and model number of FJE, and is installed according to the structure of figures 1 and 2, and consists of an end plate 1, a cylinder body 2, an evaporation tube bundle 3, a separation plate 4, a liquid inlet 5, an air outlet pipe 6 and a baffle plate 8; the end plate 1 and the steel cylinder 2 with the outer diameter phi of 500 and the length of 3000mm form a closed space, and the air outlet pipe 6 with the outer diameter phi of 100mm is close to the water outlet and vertically arranged at the upper part of the cylinder 2; the evaporation tube bundle 3 and the end plate 1 are fixed through expansion joint or welding, the partition plate 4 divides the evaporation tube bundle into an upper area and a lower area, and the flow number of the first evaporation area 301 and the second evaporation area 302 is 2 as well as that of water; the liquid inlet 5 is close to the water outlet and horizontally arranged; the baffle plate 8 is arranged in the shell, so that the refrigerant can flush the wall of the heat exchange tube along the baffle plate; the partition plate 4 is attached to the end plate 1 at one end thereof without a gap, and has a certain clearance with the end plate 1 at the other end thereof so that the refrigerant can flow from the lower region to the upper region; the interval of the baffle plates 8 becomes larger and larger in the refrigerant flow direction. The liquid inlet 5 is horizontally arranged.
In the heat exchange tube bundle zone, the refrigerant is baffled under the action of the baffle plate 8 to scour the heat exchange tube wall, as shown in fig. 3.
The refrigerant is deflected by the baffle plate 8 and the partition plate 4, and flows from the lower region to the upper region, as shown in fig. 4.
The water flows in and out from top to bottom, i.e., from right and left, downward, and then from left and right, as shown in fig. 6. Reverse flow heat exchange is formed in the direction opposite to the flow direction of the refrigerant.
Embodiment two:
fig. 7 and 8 show a combination of flow evaporators, which are stacked one above the other, with the outlet of the lower flow evaporator being the inlet of the upper flow evaporator, and which is realized by means of a line 9, the combination comprising a refrigerant liquid inlet 5 and a gas outlet 6, with baffles 8B being spaced more and more apart in the direction of the refrigerant flow, wherein the flow evaporators are free of separating plates 4.
As shown in fig. 9, the refrigerant flows in the combination of flow evaporators by the baffle 8.
The heat exchange coefficient of the invention is superior to that of a flooded evaporator and a falling film evaporator, the cost of the heat exchanger is superior to that of the falling film evaporator due to simple design and simple manufacture, and the refrigerant is in a two-phase flow state, so the refrigerant filling amount is low, about 30% of that of the flooded evaporator; because the oil flow mode is close to the dry evaporator and is carried by the gaseous refrigerant, the oil return concern is avoided, an oil return device is not needed, and the cost is low; the tube bundles can be fully distributed on the cylinder, so that the volume utilization rate of the heat exchanger is high, and the cost is low; the heat exchanger can be used for some sloshing occasions such as ship air conditioning or ice making due to the fact that the heat exchanger has no gravity. The flow type heat exchanger can be combined with the flooded evaporator besides self combination, and the refrigerant flows through the flooded evaporator first and then flows through the flow type evaporator; or in combination with a falling film evaporator, the refrigerant flows through the falling film evaporator and then through the flow evaporator.
The foregoing is a preferred embodiment of the present invention, and various changes and modifications may be made therein by those skilled in the art without departing from the general inventive concept, and such changes and modifications should be considered as falling within the scope of the claimed invention.
Claims (7)
1. A marine mobile evaporator, characterized by:
comprises a cylinder body (2), a heat exchange tube bundle (3), an air outlet pipe (6) and a liquid inlet (5);
a group of baffle plates (8) are fixed on the inner wall of the cylinder (2) in the direction perpendicular to the inner wall of the cylinder, small holes for the heat exchange tube bundles (3) to pass through are formed in the baffle plates (8), and the inside of the cylinder is partitioned into a refrigerant channel for the refrigerant to wash the heat exchange tube bundles (3) back and forth by the baffle plates (8);
the air outlet pipe (6) is vertically upwards, and the liquid inlet (5) can be arranged at any corresponding position on the cylinder (2) according to the arrangement of the refrigerant channels;
the flow direction of the non-refrigerant liquid in the heat exchange tube bundle (3) is opposite to the flow direction of the refrigerant in the cylinder (2);
the cooling device further comprises a separation plate (4), wherein the separation plate (4) separates the cylinder body (2) into at least two equal parts, each equal part forms a refrigerant flow passage, and a fan-shaped baffle plate (8) covers a part of the sectional area of the refrigerant flow passage; one end of the partition plate (4) is fixedly connected with the end plate (1), the other end of the partition plate is provided with a notch, and the notch is the communicated part of two adjacent flow channels;
the baffle plate (8) is semicircular, and the marine flow type evaporator is of a single-flow structure;
the separation plate (4) is a flat plate penetrating through the central axis of the cylinder body to separate the cylinder body into two refrigerant flow channels, the baffle plate (8) is in a 90-degree fan shape, and the refrigerant flow channels with semicircular sections are divided into two parts.
2. The marine mobile evaporator according to claim 1, wherein: the cylinder body (2) is horizontally arranged; the air outlet pipe (6) is close to the water inlet and is vertically arranged at the upper part of the cylinder body (2); the liquid inlet is close to the water outlet.
3. The marine mobile evaporator according to claim 1, wherein: the heat exchange tube bundle (3) and the end plate (1) are connected or welded and fixed through expansion, the partition plate (4) is attached to the end plate (1) at one end, a certain gap is reserved between the other end and the end plate (1), so that the refrigerant can flow from the upper area to the lower area, the partition plate (4) partitions the evaporation tube bundle, the first evaporation area (301) and the second evaporation area (302) are the same in partition number and water flow number, and the refrigerant and the water flow in the opposite direction.
4. A flow evaporator according to claim 1 wherein: the heat exchange tube bundle (3) is partitioned by a partition plate (4) in the height direction or the width direction; the gap between the other end of the partition plate (4) and the end plate (1) increases with the increase of the flow number of the refrigerant; the baffle plates (8) are spaced more and more apart along the refrigerant flow direction.
5. A method of using the flow evaporator of claim 1, wherein: when a mixture of two-phase low-pressure low-temperature refrigerant and oil enters through the liquid inlet (5), the refrigerant can only flow forwards in the partition of the heat exchange tube bundle (3) separated by the separation plate (4), and during the flowing process, the refrigerant is subjected to the action of the baffle plate to wash the heat exchange tube bundle (3), enters the next partition through the gap between the other end of the separation plate (4) and the end plate at the end of the partition, flows in the same partition, and then enters the next partition until reaching the air outlet; the partition plate (4) partitions the heat exchange tube bundle (3), wherein the number of the partitions is equal to the number of the flow paths of water and the number of the flow paths of refrigerant; the flow direction of water is opposite to the flow direction of the refrigerant, so that countercurrent heat exchange is formed; an air outlet pipe (6) of the refrigerant is close to the water inlet, so that the air outlet can have a certain superheat degree, and meanwhile, oil is sufficiently concentrated; the oil flows with the refrigerant and is eventually carried out of the system by the gaseous refrigerant.
6. A method of using the flow evaporator of claim 1, wherein: a combination of a plurality of flow evaporators as claimed in claim 1, the outlet of the preceding flow evaporator being the inlet of the next flow evaporator, the combination comprising a liquid inlet (5) and a liquid outlet (6) in a parallel or vertically stacked relative position.
7. A method of using the flow evaporator of claim 1, wherein: the flow type evaporator and the flooded evaporator are combined, the refrigerant flows through the flooded evaporator, gas rises to enter the compressor, and the rest liquid enters the flow type evaporator and is gasified to enter the compressor; alternatively, the combination of a flow evaporator and a falling film evaporator is performed, the refrigerant first flows through the falling film evaporator, the gas rises into the compressor, the remaining liquid enters the flow evaporator, and then is vaporized into the compressor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710324596.4A CN106969549B (en) | 2017-05-10 | 2017-05-10 | Marine flowing type evaporator and application method thereof |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710324596.4A CN106969549B (en) | 2017-05-10 | 2017-05-10 | Marine flowing type evaporator and application method thereof |
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| CN106969549A CN106969549A (en) | 2017-07-21 |
| CN106969549B true CN106969549B (en) | 2023-10-13 |
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| CN110285606A (en) * | 2019-07-02 | 2019-09-27 | 上海柯茂机械有限公司 | Flooded evaporator |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101311647A (en) * | 2007-05-25 | 2008-11-26 | 开利公司 | Composite type full-liquid type heat converter for refrigerant circulation system |
| CN201397057Y (en) * | 2009-05-21 | 2010-02-03 | 无锡科伦达化工热力装备有限公司 | Novel evaporator |
| CN203501563U (en) * | 2013-10-10 | 2014-03-26 | 上海瀚艺冷冻机械有限公司 | Flooded evaporator and refrigerating system including same |
| CN106091487A (en) * | 2016-07-22 | 2016-11-09 | 王言明 | A kind of cleanable heat pump heat exchanger |
| CN207065934U (en) * | 2017-05-10 | 2018-03-02 | 英得艾斯（上海）冷冻空调有限公司 | A kind of flow-type evaporator peculiar to vessel |
-
2017
- 2017-05-10 CN CN201710324596.4A patent/CN106969549B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101311647A (en) * | 2007-05-25 | 2008-11-26 | 开利公司 | Composite type full-liquid type heat converter for refrigerant circulation system |
| CN201397057Y (en) * | 2009-05-21 | 2010-02-03 | 无锡科伦达化工热力装备有限公司 | Novel evaporator |
| CN203501563U (en) * | 2013-10-10 | 2014-03-26 | 上海瀚艺冷冻机械有限公司 | Flooded evaporator and refrigerating system including same |
| CN106091487A (en) * | 2016-07-22 | 2016-11-09 | 王言明 | A kind of cleanable heat pump heat exchanger |
| CN207065934U (en) * | 2017-05-10 | 2018-03-02 | 英得艾斯（上海）冷冻空调有限公司 | A kind of flow-type evaporator peculiar to vessel |
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| CN106969549A (en) | 2017-07-21 |
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