CN210004635U

CN210004635U - kinds of condensers

Info

Publication number: CN210004635U
Application number: CN201920851134.2U
Authority: CN
Inventors: 张欣
Original assignee: Wuxi City Perseverance Reaches Equipment Ltd Waterborne
Current assignee: Wuxi City Perseverance Reaches Equipment Ltd Waterborne
Priority date: 2019-06-06
Filing date: 2019-06-06
Publication date: 2020-01-31
Anticipated expiration: 2029-06-06

Abstract

The utility model relates to an kind of condensers, including pipeline main part, two sets of interface channel, pipeline bracket and escape orifice, two sets of interface channel install respectively in the left and right sides both ends of pipeline main part, install multiunit reaction channel and condenser pipe in the pipeline main part respectively, pipeline bracket fixes the multiunit respectively reaction channel with the condenser pipe, the escape orifice process in the outer end of pipeline main part, the condenser is fixed angle right slope, solved the pipeline liquefaction effect of inside that current scheme caused unobvious, inside pipeline and cold oil contact insufficient, cold oil cooling ability weak and the inhomogeneous scheduling problem of cold oil temperature.

Description

kinds of condensers

Technical Field

The utility model relates to a mechanical equipment, concretely relates to kinds of condensers.

Background

chemical industry is an indispensable important component in national economy, and in chemical extraction, the condenser is applied to in the chemical industry, the condenser is which is the main exchange equipment of a refrigerating device, and the condenser is used in the chemical industry together with a reaction kettle, so that the required chemical materials can be obtained, gas passes through a pipeline in the condenser, the supercooled medium flows in the condenser, and the cooled medium liquefies the gas and recycles the liquid.

The existing scheme is that a plurality of groups of pipelines are arranged in a condenser, cold oil flows through the condenser, gas passes through the pipelines, the cold oil takes away heat in the pipelines, and the gas is liquefied, and the problems exist in the scheme that (1) the plurality of groups of pipelines are bound at , the liquefaction effect of the internal pipelines is not obvious, (2) the plurality of groups of pipelines are bound at , the internal pipelines are not fully contacted with the cold oil, (3) the liquefaction of the gas in the pipelines is realized through the cold oil, the cooling capacity is not strong, and (4) the cold oil enters the condenser, the gas in the pipelines is liquefied, and the temperature of the cold oil is not uniform.

SUMMERY OF THE UTILITY MODEL

The utility model discloses a not enough to prior art, the utility model discloses an kinds of condensers to solve among the prior art not obvious, inside pipeline and the cold oil contact of inside pipeline liquefaction effect insufficient, cold oil cooling ability weak and the inhomogeneous scheduling problem of temperature of cold oil.

The utility model discloses the technical scheme who adopts as follows:

A condenser, characterized by:

the pipeline comprises a pipeline main body, two groups of connecting channels, a pipeline support and a drain outlet, wherein the two groups of connecting channels are respectively installed at the left end and the right end of the pipeline main body, a plurality of groups of reaction channels and condensation pipes are respectively installed in the pipeline main body, the pipeline support is used for fixing the plurality of groups of reaction channels and condensation pipes respectively, the drain outlet is processed at the outer end of the pipeline main body, and the condenser is and inclines rightwards.

, the condenser inclines rightwards at an angle of 5-7 degrees.

, two groups of pipeline seal plates are respectively processed at the left end and the right end of the pipeline main body, and the left end and the right end of the reaction channel respectively penetrate through the two groups of pipeline seal plates.

, installing multiple groups of reaction channels in the main pipeline body from top to bottom in parallel, wherein the lengths of the multiple groups of reaction channels are the same as the length of the main pipeline body, and gaps are reserved among the multiple groups of reaction channels.

, the reaction channel is cuboid.

, the technical proposal is that the condensation pipe is a hollow pipe and cooling liquid flows through the condensation pipe.

, the condenser also comprises an air intake device which is arranged at the outer end of the pipeline main body and is arranged at the upper end of the discharge outlet.

, the air intake device is a motor fan.

the technical proposal is that the outer surface of the pipeline main body is wrapped with an insulating layer.

The beneficial effects of the utility model are that the utility model discloses an reaction channel that the condenser adopted the cuboid shape, increased reaction area, adopt the condensation to reduce the temperature in the condenser admittedly, adopt hot blast blowpipe apparatus to make the temperature in the condenser even, the condenser has brought following effect (1) the reaction channel of cuboid shape, reaction area has been increased, reaction efficiency has been accelerated, (2) there is the clearance between the multiunit reaction channel, reaction channel and air conditioning reaction are abundant, (3) reduce the temperature in the condenser through the condenser pipe, the cooling capacity of condenser pipe is strong, (4) air inlet apparatus blows to the condenser, the temperature of air conditioning is even, (5) the pipe bracket is fixed reaction channel and condenser pipe, the going on of reaction has been guaranteed.

Drawings

Fig. 1 is a schematic structural diagram of the present invention.

Fig. 2 is a cross-sectional view taken at a in fig. 1.

In the figure: 1. a pipe body; 11. a pipeline closing plate; 2. a connecting channel; 3. a reaction channel; 4. a condenser tube; 5. a pipe support; 6. a drain port; 7. an air intake device; 8. and (7) an insulating layer.

Detailed Description

The following describes a specific embodiment of the present embodiment with reference to the drawings.

Fig. 1 is the utility model discloses a schematic structure diagram, fig. 2 is the A department's section view of fig. 1, it is shown with fig. 2 to combine, the utility model discloses an kinds of condensers, the direction of X does in the picture the utility model discloses schematic structure diagram's upper end, the direction of Y does in the picture the utility model discloses schematic structure diagram's right-hand member condenser includes pipeline main part 1, two sets of interface channel 2, pipe bracket 5 and escape orifice 6.

The duct body 1 is a hollow duct. Preferably, the pipe body 1 is cylindrical. Two groups of pipeline closing plates 11 are respectively processed at the left end and the right end of the pipeline main body 1. A plurality of groups of reaction channels 3 and condensing tubes 4 are respectively arranged in the pipeline main body 1. The left and right ends of the reaction channels 3 respectively pass through the two groups of pipeline closing plates 11. Preferably, the tunnel closure plate 11 is circular.

Two sets of duct seal plates 11 seal the duct body 1 from the left and right ends of the duct body 1. So that the heat exchange reaction of the condenser can be stably performed in the tube main body 1. Two sets of pipeline shrouding 11 seal pipeline main part 1, make pipeline main part 1 can not take place to reveal.

The two sets of connecting channels 2 are respectively arranged at the left end and the right end of the pipeline main body 1. Preferably, the connecting channel 2 is semicircular. The left end of the pipeline main body 1 is an air inlet end, and the right end of the pipeline main body 1 is a liquid outlet end. The inner ends of the two groups of connecting channels 2 are respectively connected with the air inlet end and the liquid outlet end. The outer ends of the two groups of connecting channels 2 are respectively connected with an external air inlet pipeline and an external liquid outlet pipeline. The inner end diameter of the connecting passage 2 is the same as the diameter of the pipe body 1. The diameter of the inner end of the connecting channel 2 is larger than the diameter of the outer end of the connecting channel 2.

groups of connecting channels 2 are responsible for conveying gas into the pipeline main body 1, the other groups of connecting channels 2 are responsible for conveying liquid discharged by the pipeline main body 1 to an external liquid outlet pipeline in a centralized manner, the two groups of connecting channels 2 are respectively connected with the left end and the right end of the pipeline main body 1 through flanges, and the flange connection ensures the connection stability of the two groups of connecting channels 2 and the pipeline main body 1.

The plurality of reaction channels 3 are arranged in parallel from bottom to bottom in the pipe body 1. The lengths of the plural sets of reaction channels 3 are the same as the length of the tube main body 1. Gaps exist between the plural sets of reaction channels 3. Preferably, the reaction channel 3 is a rectangular parallelepiped. The reaction channel 3 is a hollow channel.

The gas enters from the left end of the reaction channel 3, and the gas is concentrated at the upper end of the inner surface of the reaction channel 3. The gas is liquefied in the reaction channel 3, and the liquid is concentrated on the lower end of the inner surface of the reaction channel 3. The liquid flows out from the right end of the reaction channel 3.

Compared with the combination of circular pipelines, the reaction channel 3 is a cuboid, the gas quantity entering the reaction channel 3 is more, the liquefaction reaction time of the reaction channel 3 is shorter, the circular pipelines are arranged by binding the circular pipelines at , the aim of the method is to put more circular pipelines and improve the reaction efficiency, but the circular pipelines bound inside are slow in liquefaction reaction, the whole liquefaction efficiency is not improved, the reaction speed is well guaranteed due to the arrangement and installation mode of the reaction channel 3, and the reaction efficiency is guaranteed due to the fact that the reaction channel 3 is a cuboid.

The condensation pipe 4 is a hollow pipe. The cooling liquid flows in the condensation pipe 4. The choice of cooling fluid is well known and can be selected by the person skilled in the art according to the operation of the device, for example R-600 refrigerant. The condensation duct 4 is installed inside the duct body 1. The condensation duct 4 does not come into contact with the reaction channel 3. The condensation duct 4 is installed at a position intermediate between the reaction channel 3 and the inner surface of the tube main body 1. Preferably, the number of the condensation ducts 4 is two. The two condensation pipes 4 are respectively installed at the front and rear ends inside the duct body 1.

The contact of the condensation pipe 4 with the reaction channel 3 may cause the frost crack of the reaction channel 3, which affects the reaction efficiency. The condensation duct 4 does not come into contact with the reaction channel 3. The condensation tube 4 does not freeze the liquid in the reaction channel 3. The normal operation of the reaction is ensured.

The pipeline bracket 5 is respectively fixed with a plurality of groups of reaction channels 3 and condensing pipes 4. In order to ensure that the reaction channel 3 works properly, no breakage occurs. The tube support 5 needs to support a plurality of sets of reaction channels 3. The pipe bracket 5 also needs to fix the condensation pipe 4. The duct bracket 5 is installed inside the duct main body 1. The pipe bracket 5 is coupled to the inner surface of the pipe body 1.

The pipe bracket 5 fixes the plurality of sets of reaction channels 3 and the condensation pipes 4, respectively, and the plurality of sets of reaction channels 3 and the condensation pipes 4 do not contact each other due to deviation. The offset of the sets of reaction channels 3 and condenser tubes 4 also affects the efficiency of the condenser.

The drain opening 6 is formed in the outer end of the pipe body 1. The drain port 6 is formed at the right end of the lower surface of the duct body 1. The drain port 6 is connected to a drain pipe. The drain port 6 communicates with the inside of the duct main body 1.

When the condenser is in operation, the liquefaction of the gas in the reaction channel 3 releases a large amount of heat. The heat is liquefied after contacting with the cold air in the pipeline body 1. Liquid will accumulate in the reaction channel 3. The liquid accumulates at the lower end inside the reaction channel 3. The liquid does not contact the condensation duct 4. The liquid is discharged through the drain 6.

The condenser also comprises an air intake device 7. The air intake device 7 is arranged at the outer end of the pipeline main body 1. The air intake device 7 is installed at the upper end of the outer surface of the pipeline main body 1. The air intake device 7 penetrates the outer surface of the duct main body 1. The air intake device 7 is installed at the upper end of the drain opening 6. Preferably, the air intake device 7 is a motor fan. The selection of the type of the motor fan is well known and can be selected by those skilled in the art according to the working condition of the device, for example, the type YWF-200-750 motor fan can be selected.

The function of the air inlet device 7 ensures the uniformity of the temperature in the pipeline main body 1. Preventing local supercooling. The air inlet device 7 blows air into the pipeline main body 1, and cold air circulates in the pipeline main body 1.

The outer surface of the pipeline main body 1 is wrapped with an insulating layer 8. The heat preservation layer 8 plays a role in heat preservation. The heat preservation layer 8 ensures the temperature of the cold air in the pipeline main body 1.

The condenser is inclined rightwards at an angle of degrees, the condenser is inclined rightwards at an angle of 5-7 degrees, and the condenser is inclined towards the right end of the condenser at an angle of 5-7 degrees with the horizontal line.

The condenser is inclined to the right at an angle of , the reaction channel 3 is also inclined to the right, after the gas in the reaction channel 3 is liquefied, the liquid flows through the right end of the reaction channel 3 through the reaction channel 3, the pipeline body 1 is also inclined to the right, the liquid accumulated in the pipeline body 1 is accumulated at the right end of the interior of the pipeline body 1, and the liquid accumulated in the pipeline body 1 flows out through the drain outlet 6.

In the present embodiment, the air intake device 7 is described as a motor fan, but the present invention is not limited thereto, and other air intake devices may be used as long as the functions thereof can be exerted.

In the present specification, terms such as "cylindrical", "circular" and "semicircular" are used, and they are not exactly "cylindrical", "circular" and "semicircular", and may be in a state of "substantially cylindrical", "substantially circular" and "substantially semicircular" within a range capable of exerting the functions thereof.

The above description is for the purpose of explanation and not limitation of the invention, which is defined in the claims, and any modifications may be made without departing from the basic structure of the invention.

Claims

The condenser is characterized by comprising a pipeline main body (1), two groups of connecting channels (2), a pipeline support (5) and a drain outlet (6), wherein the two groups of connecting channels (2) are respectively installed at the left end and the right end of the pipeline main body (1), a plurality of groups of reaction channels (3) and condensation pipes (4) are respectively installed in the pipeline main body (1), the pipeline support (5) is used for respectively fixing a plurality of groups of reaction channels (3) and condensation pipes (4), the drain outlet (6) is processed at the outer end of the pipeline main body (1), and the condenser is inclined rightwards at a fixed angle of degrees.
2. The condenser of claim 1, wherein: the condenser is inclined rightwards at an angle of 5-7 degrees.
3. The condenser of claim 1, wherein: two groups of pipeline closing plates (11) are respectively processed at the left end and the right end of the pipeline main body (1); the left end and the right end of the reaction channel (3) respectively penetrate through the two groups of pipeline closing plates (11).
4. The condenser of claim 1, wherein: a plurality of groups of reaction channels (3) are arranged in the pipeline main body (1) in parallel from top to bottom; the lengths of the reaction channels (3) are the same as the length of the pipeline main body (1); gaps exist among a plurality of groups of the reaction channels (3).
5. The condenser of claim 1, wherein: the reaction channel (3) is a cuboid.
6. The condenser of claim 1, wherein: the condensation pipe (4) is a hollow pipeline; the cooling liquid flows in the condensation pipe (4).
7. The condenser of claim 1, wherein: the condenser also comprises an air inlet device (7); the air inlet device (7) is arranged at the outer end of the pipeline main body (1); the air inlet device (7) is arranged at the upper end of the drain outlet (6).
8. The condenser of claim 7, wherein: the air inlet device (7) is a motor fan.
9. The condenser of claim 1, wherein: the outer surface of the pipeline main body (1) is wrapped with an insulating layer (8).