KR102372633B1 - Removable siphon with neutralizer tank - Google Patents

Abstract

The present invention relates to a siphon capable of attaching and detaching a neutralizer tank, having a flow path formed therein, and having a gas oil pipe having upper and lower connection pipes formed on the outer surface and the lower part, and one end is exposed above the gas oil pipe, the other end is Forming an inlet pipe coupled to be located in the diesel pipe, having an exhaust pipe integrally extending from the top of the diesel pipe, sealing the lower end of the diesel pipe with a bottom cap, depending on the acidity concentration of the condensed water flowing into the diesel pipe, upper and lower It is possible to attach or detach the neutralizer tank that discharges condensed water as it is through the discharge pipe or neutralizes and discharges the neutralizer tank by determining whether to attach or detach the neutralizer tank to the connection pipe.
According to the present invention, the neutralizer tank can be selectively installed in the upper and lower connection pipes according to the acid concentration of the condensate, and the upper and lower connection pipes are sealed with a sealing stopper, so that the condensed water can be discharged through the discharge pipe as it is, and the diesel pipe By discharging the condensed water in it as it is through the discharge pipe, the condensed water discharge time can be shortened, and the time that the condensed water stays in the gas oil pipe is reduced, thereby preventing foreign substances or moss from being generated in the gas oil pipe and the discharge pipe, and the volume By installing a reduced siphon in the boiler, the volume of the boiler is reduced at the same time, and by connecting the neutralizer tank to the upper and lower connection pipes, it is possible to reduce the acid concentration of the condensate discharged through the discharge pipe.

Description

Removable siphon with neutralizer tank

The present invention relates to a siphon, and more particularly, to a siphon capable of attaching and detaching a neutralizer tank capable of attaching and detaching the neutralizer tank by connecting the neutralizer tank to the upper and lower connection tubes of the diesel tube or closing it with a sealing stopper.

In general, the principle of a boiler is that it absorbs sensible heat first and absorbs latent heat emitted as exhaust gas secondarily. By recovering heat at about ℃, it is possible to obtain high heat of 95% or more.

And, in such a heat absorption type boiler, the water vapor contained in the exhaust gas is condensed below the dew point temperature and discharged to the outside of the heat exchanger. If it comes into contact with parts, there is a risk of corrosion, and if the acidic condensate is discharged directly into the sewer, there is a risk of environmental pollution.

Therefore, in order to prevent such condensed water from causing corrosion or other environmental pollution problems, a dilution method of increasing the PH by supplying a certain amount of dilution water to the condensed water was used in Europe and Japan.

Patent Document 1 shows the condensate siphon structure of a conventional boiler. Referring to this,

A siphon having a hollow shape accommodating the neutralizing member therein, a siphon having an outlet on one side of the lower end, an upper cover covering the upper part of the siphon, and an upper cover having an inlet communicating with the storage room on the upper surface, and the upper part A partition wall extending from the upper end of the cover and the storage chamber in the lower longitudinal direction to partition the storage room space, and forming an open hole at the lower end thereof, and a periphery of the discharge unit protruding upward at a predetermined height from the bottom of the periphery of the discharge unit, the neutralizing member It consists of a mesh part that blocks the inflow in the direction of the discharge part.

Here, the mesh part protrudes further downward from the bottom surface of the upper cover, and the mesh part protruding from the bottom of the storage chamber and the mesh part protruding from the bottom surface of the upper cover are engaged with each other.

At this time, the blocking pieces of the mesh part formed to be symmetrical to each other up and down are engaged with each other, and accordingly, the condensed water in the storage room overflows in the direction of the discharge part through the hole formed between the blocking pieces.

In addition, the partition wall portion is formed to be positioned between the inlet portion and the mesh portion, and guides the condensed water flowing in through the inlet portion to be supplied in one direction of the storage chamber.

That is, when condensed water is supplied through the inlet, the condensed water is filled to a predetermined water level in the storage chamber, and in that state, the acidity is gradually lowered by being purified by the neutralizing member.

And, when the condensed water of a predetermined amount or more is filled in the storage room, the purified condensed water is moved to the other direction of the storage room through the open hole, and then passes over the mesh part and moves toward the discharge part through the hole between the blocking pieces. , is discharged through the outlet.

At this time, the neutralizing member floating in proportion to the amount of condensed water is blocked by the blocking piece of the mesh part to prevent it from flowing into the discharge part.

However, Patent Document 1 as described above has the inconvenience of having to discharge the condensed water to the discharge part through the storage room in which the neutralizing member is necessarily accommodated regardless of the acid concentration of the condensate, and The condensed water stays in the storage room until it is reached, delaying the condensate discharge time. Also, in the case of a boiler with a small amount of usage, the condensed water residence time in the storage room becomes longer and the moss generation rate increases on the inner wall or floor of the storage room, especially, By increasing the storage room area to be proportional to the capacity of the neutralizing member, the volume of the siphon is increased, and by forming a space proportional to the size of the siphon inside the boiler, the volume area of the boiler is increased, thereby reducing the reliability of the product there is.

KR 20-0362891 Y1

The present invention is to solve the above-described problems, and an object of the present invention is to form a flow path inside, and to have a light oil pipe having upper and lower connecting pipes formed on the outer surface and the lower part, and one end is above the light oil pipe The condensate acid concentration of condensate flowing into the diesel pipe by forming an inlet pipe coupled so that the other end is located in the diesel pipe is provided, and an exhaust pipe integrally extending from the top of the diesel pipe, and sealing the lower end of the diesel pipe with a lower cap. Accordingly, it is to provide a siphon capable of attaching and detaching the neutralizer tank, which determines whether the neutralizer tank is detached or attached to the upper and lower connection pipes, and discharges condensed water as it is through the discharge pipe, or neutralizes and discharges the neutralizer tank.

In order to achieve the object of the present invention as described above, the siphon capable of attaching and detaching a neutralizer tank according to the present invention has a hollow tubular body shape with an open bottom, a flow path is formed inside, and upper and lower connections are made on the outer surface and the lower part. a pass-through tube forming a tube; an inlet pipe having a hollow tubular shape, one end exposed above the light oil pipe, the other end being coupled to be positioned in the flow path of the light oil pipe, and supplying condensed water into the flow path; a discharge pipe extending integrally with the upper end of the light oil pipe and communicating with the flow path of the light oil pipe; It characterized in that it is composed of a; is fixed to the lower end of the gas oil pipe, the lower cap for sealing the lower part of the gas oil pipe.

In the detachable siphon of the neutralizer tank according to the present invention, the lower end of the gas oil pipe is formed to have a lower height than the lower end of the inlet pipe, so that the condensed water introduced through the inlet pipe is the flow path of the gas oil pipe. It is characterized in that it guides to be supplied.

In the siphon capable of attaching and detaching the neutralizer tank according to the present invention, the gas oil pipe is press-fitted to each of the upper and lower connecting pipes, and a sealing stopper for sealing the upper and lower connecting pipes communicating with the flow path is further formed. characterized.

In the detachable siphon of the neutralizing agent tank according to the present invention, the light oil pipe has a hollow tubular shape, has a neutralizer inside, and is connected to the upper and lower connecting pipes on one side and at the bottom in communication with the flow path. A neutralizer tank having an outlet and an inlet to be connected is further formed, and the flow path between the gas oil pipe and the inlet pipe is fixedly fitted to be positioned between the outlet and the inlet of the neutralizer tank, the flow path between the outlet and the inlet By blocking the lower end cap, it characterized in that a blocking partition wall is further formed to block the movement of the condensed water in the flow path in the direction of the outlet.

In the siphon capable of attaching and detaching the neutralizer tank according to the present invention, the flow path of the light oil pipe is divided into upper and lower flow channels based on the blocking partition wall.

In the siphon capable of attaching and detaching a neutralizer tank according to the present invention, the gas oil pipe is recessed along the inner peripheral surface, allowing the blocking partition wall to be caught, so that the blocking partition wall is positioned between the gas oil pipe and the inlet pipe, It is characterized in that it further forms a stepped groove to block the flow down.

In the detachable siphon of the neutralizing agent tank according to the present invention, the lower cap is formed to protrude upward between the light oil pipe and the inlet pipe and is positioned in the flow path, and a predetermined distance is spaced along the outer surface of the protruding wall part. to further form a through-hole allowing the condensed water introduced through the inlet pipe to be supplied into the flow path of the light oil pipe, and the protruding wall portion allows the blocking partition wall to be fitted and fixed to the upper end thereof, the blocking partition wall It is characterized in that it is supported so as to be positioned in the flow path between the upper connection pipe and the lower connection pipe.

In the detachable siphon of the neutralizer tank according to the present invention, the neutralizer tank is fastened to surround the outer surface of the outlet or the inlet, and a connection frame connecting the outlet and the upper connecting pipe or the inlet and the lower connecting pipe. It is characterized in that it is formed further.

In the detachable siphon of the neutralizer tank according to the present invention, the discharge pipe is formed integrally extending from the upper end of the light oil pipe in a downwardly inclined direction.

According to the present invention, the neutralizer tank can be selectively installed by removing and attaching the neutralizer tank to the upper and lower connection pipes according to the acid concentration of the condensate. By sealing, the condensate can be discharged as it is through the discharge pipe, and the condensed water that has risen to a predetermined height in the diesel pipe is discharged as it is through the discharge pipe, so that the condensate discharge time can be shortened. This is reduced to prevent the generation of foreign substances or moss in the pipeline, and by installing a siphon with a reduced volume in the boiler, the volume of the boiler is reduced at the same time, and in particular, when the condensate acid concentration is higher than a predetermined concentration, the upper and lower By connecting the neutralizer tank to the connecting pipe, it is possible to reduce the acid concentration of the condensate discharged through the discharge pipe. Accordingly, the use of the neutralizer tank can be selected according to the surrounding environmental requirements when installing the boiler, so the reliability of the product is improved. There is this.

1 is a perspective view showing a siphon capable of attaching and detaching a neutralizer tank according to the present invention.
Figure 2 is an exploded perspective view of Figure 1;
3 is a cross-sectional view taken along AA of a siphon capable of attaching and detaching a neutralizer tank according to the present invention.
4 is a cross-sectional view taken along BB of a siphon capable of attaching and detaching a neutralizer tank according to the present invention.
5 is a perspective view of a cleaning agent tank installed on a detachable siphon of a neutralizing agent tank according to the present invention.
Figure 6 is an exploded perspective view of Figure 5;
7 is a cross-sectional view taken along CC of a siphon capable of attaching and detaching a neutralizer tank according to the present invention.

Hereinafter, embodiments of the present invention will be described in more detail with reference to the accompanying drawings.

1 to 7, the light oil pipe 100 has a hollow tubular body shape with an open lower part, and forms a flow path 101 inside, and upper and lower connection pipes 100a and 100b on the outer surface and the lower part. to form

The light oil pipe 100 guides the condensed water flowing in through the inlet pipe 200 to move in the direction of the discharge pipe 300 .

The diameter of the flow path 101 of the light oil pipe 100 is formed to be relatively larger than the outer diameter of the inlet pipe 200, and the inflow pipe 200 is accommodated therein.

The gas oil pipe 100 has a lower end height that is relatively lower than the lower end height of the inlet pipe 200 , so that the condensed water introduced through the inlet pipe 200 flows into the flow path 101 of the gas oil pipe 200 . ) to be supplied.

The light oil pipe 100 receives the condensed water to the lower portion of the flow path 101 through the inlet pipe 200, and guides the condensed water to move upward.

The lower end of the light oil pipe 100 is closed by the lower cap 400 .

The light oil pipe 100 is press-fitted to each of the upper and lower connecting pipes 100a and 100b to seal the upper and lower connecting pipes 100a and 100b communicating with the flow path 101. A sealing stopper (102) to form more

The sealing stopper 102 blocks the condensed water moving along the flow path 101 from being discharged to the outside through the upper and lower connection pipes 100a and 100b.

The sealing stopper 102 is preferably made of a rubber material.

The gas oil pipe 100 has a hollow tubular shape, has a neutralizer 104 therein, and is in communication with the flow path 101 on one side on one side and on the lower side, respectively. A neutralizer tank 103 having an outlet 103a and an inlet 103b to be connected is further formed, and in the flow path 101 between the light oil pipe 100 and the inlet pipe 200, the neutralizer tank 103 It is fitted and fixed to be positioned between the outlet 103a and the inlet 103b of the A blocking partition wall 105 for blocking the movement of the condensed water in the closed flow path 101 in the direction of the outlet 103a is further formed.

The neutralizing agent tank 103 allows the condensed water introduced into the gas oil pipe 100 to pass through the neutralizing agent 104 to neutralize the acidic concentration of the condensed water.

The flow passage 101 of the light oil pipe 100 is divided into upper and lower flow passages 101a and 101b based on the blocking partition wall 105 .

The upper flow passage 101a accommodates neutralized condensed water having an acidic concentration value that is relatively lower than a predetermined acid concentration value, and the lower flow passage 101b corresponds to the predetermined acid concentration value or is relatively higher than the predetermined acid concentration value. Condensate with an acidic concentration value is received.

The outlet 103a and the inlet 103b of the neutralizer tank 103 are coupled to communicate with each of the upper connecting pipe 100a and the lower connecting pipe 100b of the light oil pipe 100 .

The neutralizer tank 103 allows the condensed water accommodated in the lower flow path 101b to be supplied to the inlet 103b through the lower connection pipe 100b based on the blocking partition wall 105, and the outlet 103a ) so that the neutralized condensed water discharged to the upper flow path 101a is discharged through the upper connection pipe 100a.

The neutralizer tank 103 is fastened to surround the outer surface of the outlet 103a or the inlet 103b, and the outlet 103a and the upper connecting pipe 100a or the inlet 103b and the lower connecting pipe 100b) A connection frame 103c for connecting them is further formed.

The connecting frame 100a integrally surrounds the outlet 103a and the upper connecting pipe 100a or the inlet 103b and the lower connecting pipe 100b so that the outlet 103a and the upper connecting pipe 100a or the It is fixed between the inlet (103b) and the lower connection pipe (100b).

The connecting frame 103c is preferably formed in a “C” shape.

The blocking partition wall 105 blocks the upward movement of the condensed water introduced into the flow path 101 through the inlet pipe 200, and at the same time, the neutralizer tank 103 through the lower connection pipe 100a. ) guide to flow into the inlet (103b).

The gas oil pipe 100 is recessed along the inner circumferential surface, allowing the blocking partition wall 105 to be caught, so that the blocking partition wall 105 is formed between the gas oil pipe 100 and the inlet pipe 200. , further to form a stepped groove portion (100c) to block the flow down.

The height of the stepped groove portion 100c is proportional to the height of the blocking barrier rib 105 , but the depth thereof is formed to be proportional to the diameter of the blocking barrier rib 105 .

The stepped groove portion 100c is formed on the inner circumferential surface between the upper and lower connection pipes 100a and 100b, and connects the blocking partition wall 105 to the flow path 101 between the upper and lower connection pipes 100a and 100b. Fix it.

The blocking partition wall 105 is fitted and fixed to the upper end of the protruding wall portion 401 of the lower cap 400 , and is supported by the protruding wall portion 401 .

The inlet pipe 200 has a hollow tubular shape, and one end is exposed above the gas oil pipe 100 , and the other end is coupled to be located in the flow path 101 of the gas oil pipe 100, and condensed water is transferred to the flow path 101 . supply to me

It is preferable that the upper end of the inlet pipe 200 is bent.

The lower end of the inlet pipe 200 communicates with the flow path 101 or with the lower flow path 101b partitioned by the blocking partition wall 105 .

The inlet pipe 101 is formed so that the lower end thereof is spaced apart from the lower end cap 400 coupled to the lower end of the light oil pipe 100 by a predetermined distance.

The inlet pipe 200 receives condensed water through an upper portion and discharges the condensed water into the flow path 101 .

The inlet pipe 200 is formed to have an outer diameter smaller than the inner circumferential diameter of the flow path 101, and guides the condensed water to fill the space therebetween.

The discharge pipe 300 is integrally formed on the upper end of the light oil pipe 100 and communicates with the flow path 101 of the light oil pipe 100 .

The discharge pipe communicates with the flow path 101 or the upper flow path 101a partitioned by the blocking partition wall 105 .

The discharge pipe 300 guides the condensed water moving upward through the flow path 101 to be discharged to the outside of the light oil pipe 100 .

The discharge pipe 300 is integrally formed so as to face a downward sloping direction from the top of the light oil pipe 100 .

The discharge pipe 300 receives the condensed water and discharges it downward.

The discharge pipe 300 is formed in a direction perpendicular to the upper and lower connection pipes 100a and 100b to prevent interference with the upper and lower connection pipes 100a and 100b.

The lower cap 400 is coupled and fixed to the lower end of the light oil pipe 100 to seal the lower portion of the light oil pipe 100 .

The lower cap 400 blocks the condensed water discharged into the flow path 101 through the inlet pipe 200 from being discharged to the outside through the lower end of the gas oil pipe 100 .

The lower cap 400 further forms an O-ring (O) on its outer peripheral surface.

The O-ring (O) is pressed and fixed between the lower end of the lower cap 400 and the light oil pipe 100, and condensed water leaks through the gap between the lower cap 400 and the light oil pipe 100. block

The lower cap 400 is formed to protrude upward between the gas oil pipe 100 and the inlet pipe 200 and includes a protruding wall part 401 positioned in the flow path 101 and an outer surface of the protruding wall part 401 . The through-holes 402 are further formed to be spaced apart from each other by a predetermined interval and allow the condensed water introduced through the inlet pipe 200 to be supplied into the flow path 101 of the light oil pipe 100 .

The protrusion wall part 401 is located in the lower flow path 101b partitioned by the flow path 101 or the blocking partition wall 105 .

The height of the upper end of the protruding wall portion 401 is preferably proportional to the height of the stepped groove portion 100c of the light oil pipe 100 .

The protruding wall portion 401 has an open upper end, and guides the condensed water to move upward through the upper end.

The through hole 402 is preferably formed to face the lower connection pipe 100b of the light oil pipe 100 .

The protrusion wall part 401 allows the blocking partition wall 105 to be fitted and fixed to the upper end thereof, so that the blocking partition wall 105 is a flow path 101 between the upper connection pipe 100a and the lower connection pipe 100b. ) to be supported.

The siphon capable of attaching and detaching the neutralizer tank according to the present invention configured as described above is used as follows.

In the following description, the concentration of condensed water generated in the boiler (not shown) may be changed to correspond to the boiler (not shown) driving environmental conditions or the type of the boiler, and in the following, the frequency or use of the boiler (not shown) It will be explained with an example that the acid concentration of the condensate is relatively high and low based on a relatively long time or a relatively short time.

First, the concentration of the condensed water generated in the boiler (not shown) is calculated, and when the acidic concentration of the condensed water is less than or equal to a predetermined concentration, the sealing plug is placed on the upper and lower connection pipes 100a and 100b of the inlet pipe 200 . (102) is pressed to close the upper and lower connecting pipes (100a, 100b).

Then, the lower end cap 400 is fitted to the lower end of the light oil pipe 100 to seal the lower end of the light oil pipe 100 .

At this time, an O-ring (O) is installed between the lower end of the lower cap 400 and the lower end of the light oil pipe 100 , and the space between the lower end cap 400 and the lower end of the light oil pipe 100 is sealed.

Here, the lower cap 400 opens the upper end to form the protruding wall portion 401 that enters the flow path 101, and allows condensed water to pass through the outer surface of the protruding wall portion 401 in the flow path 101 direction. A through hole 402 is formed.

In addition, the gas oil pipe 100 in which the inlet pipe 200 and the outlet pipe 300 are integrally formed is positioned inside the boiler (not shown), and the upper end of the inlet pipe 200 is connected to a condensate drip tray (not shown) and connected, and the discharge pipe 300 is coupled to be exposed to the lower part of the boiler (not shown).

At this time, the discharge pipe 300 is formed to be inclined downward from the upper end of the gas oil pipe 100 to maintain a state in communication with the flow path 101 of the gas oil pipe 100 .

Then, when the boiler (not shown) is driven, the exhaust gas generated during combustion is discharged to the outside of the boiler, condensed water is accommodated in the condensate gutter (not shown), and the condensed water falls to the lower part of the condensate gutter (not shown). and is supplied to the inlet pipe 200 .

At this time, the acidic concentration of the condensed water supplied to the inlet pipe 200 is condensed water having a relatively lower concentration value than the predetermined acidic concentration.

Then, the condensed water introduced through the upper end of the inlet pipe 200 is guided to the inlet pipe 200 and discharged to the lower end of the inlet pipe 200 , so that the light oil pipe communicated with the inlet pipe 200 . Condensed water is supplied into the flow path 101 of the 100 , and the condensed water is accommodated in the light oil pipe 100 .

At this time, the condensed water received into the flow path 101 of the light oil pipe 100 gradually fills up in the flow path 101 through the through hole 402 and the open upper part of the lower cap 400 .

In particular, this condensed water is blocked by the sealing stopper 102 that seals the upper and lower connecting pipes 100a and 100b, and accordingly, the light oil pipe 100 through the upper and lower connecting pipes 100a and 100b. It is blocked from being discharged to, and rises to a water level corresponding to the position of the discharge pipe 300 connected to the upper end of the gas oil pipe 100 in the flow path 101 .

And, the condensed water that has risen to correspond to the height of the discharge pipe 300 communicating with the flow path 101 overflows into the discharge pipe 300 , and accordingly, the condensed water accommodated in the flow path 101 is passed through the discharge pipe 300 . It is discharged to the outside of the boiler (not shown).

On the other hand, the concentration of the condensed water generated in the boiler (not shown) is calculated, and when the acidic concentration of the condensed water is greater than or equal to a predetermined concentration, the neutralizing agent is applied to each of the upper and lower connection pipes 100a and 100b of the inlet pipe 200 . By connecting the outlet 103a and the inlet 103b of the tank 103, the upper and lower connecting pipes 100a and 100b and the outlet 103a and the inlet 103b are in communication.

At this time, the neutralizing agent tank 103 accommodates the neutralizing agent 104 therein.

Then, the connecting frame 103c is fastened so as to surround the inlet 103b and the outlet 103a of the neutralizer tank 103, and the inlet 103b and the lower connecting pipe 100b are connected to the connecting frame 103c. And between the outlet (103a) and the upper connection pipe (100a) is fixed by tightening.

Here, the connection frame 103c is fastened in a "C" shape to fasten and fix the inlet 103b, the lower connection pipe 100b, and the outlet 103a and the upper connection pipe 100a.

In addition, the blocking partition wall 105 is inserted through the open lower part of the light oil pipe 100, and the blocking partition wall 105 is moved upward along the flow path 101 so that the blocking partition wall 105 is the To be located in the stepped groove portion (100c) of the light oil pipe (100).

Then, the outer surface of the blocking partition wall 105 is caught in the stepped groove portion 100c, so that it is fixed on the flow path 101 between the upper and lower connection tubes 100a and 100b of the gas oil pipe 100, and the The flow path 101 of the light oil pipe 100 is divided into upper and lower flow paths 101a and 101b.

Then, the lower cap 400 is inserted and coupled to the lower end of the light oil pipe 100 so that the upper end of the protruding wall portion 401 of the lower cap 400 is fitted and fixed to the lower surface of the blocking partition wall 105 and at the same time The through hole 402 is fixed to face the lower connection pipe 100b.

At this time, the blocking partition wall 105 is supported by the protruding wall portion 401 in a state where it is caught in the stepped groove portion 100c.

In addition, the O-ring (O) is installed between the lower end of the gas oil pipe 100 and the lower end cap 400 as described above, thereby sealing the space between the lower end of the gas oil pipe 100 and the lower end cap 400 .

Then, when the boiler (not shown) is driven, the exhaust gas generated during combustion is discharged to the outside of the boiler (not shown), and condensed water is accommodated in the condensed water gutter (not shown), and the condensed water is stored in the condensed water gutter (not shown). ) falls down and is supplied to the inlet pipe 200 .

In this case, the acidic concentration of the condensed water supplied to the inlet pipe 200 is condensed water corresponding to the predetermined acidic concentration or having a relatively higher concentration than the predetermined acidic concentration.

Then, the condensed water introduced through the upper end of the inlet pipe 200 is guided to the inlet pipe 200 and discharged to the lower end of the inlet pipe 200 , so that the light oil pipe communicated with the inlet pipe 200 . The condensed water is supplied into the lower passage 101b of 100, and the condensed water is accommodated in the lower passage 101b.

At this time, the condensed water received in the lower flow path 101b moves to the inlet 103b of the neutralizer tank 103 through the lower connection pipe 100b.

Here, it is preferable that the level of the condensed water accommodated in the lower flow path 101b is proportional to the level of the condensed water accommodated in the neutralizing agent tank 103 .

At this time, when the water level of the condensed water reaches the bottom surface of the blocking partition wall 105, the condensed water is restricted from being received in the lower flow passage 101b, and at the same time, the condensed water level in the neutralizing agent tank 103 is lowered to the lower flow passage 101b. ) is formed to be relatively higher than the level of the condensed water, and is filled to a water level corresponding to the height of the outlet (103a).

In particular, the condensed water accommodated in the neutralizing agent tank 103 through the inlet 103b is neutralized by the neutralizing agent 104 accommodated in the neutralizing agent tank 103, and the acidity concentration is reduced below a predetermined concentration value.

And, the condensed water neutralized in the neutralizing agent tank 103 is discharged in the direction of the upper connection pipe 100a through the outlet 103a, and the condensed water is accommodated in the upper flow path 101a.

At this time, the blocking partition wall 105 blocks the condensed water accommodated in the upper passage 101a from leaking into the lower passage 101b.

Thereafter, as the condensed water is continuously filled in the upper flow path 101a based on the blocking partition wall 105 as described above, the condensed water is filled in the neutralizing agent tank 103, and the condensed water capacity in the neutralizing agent tank 103 is continuously filled. After this is exceeded, the condensed water fills up to a water level corresponding to the height of the discharge pipe 300 connected to the upper end of the light oil pipe 100 .

And, the condensed water that has risen to correspond to the height of the discharge pipe 300 communicating with the upper flow path 101a overflows into the discharge pipe 300, and accordingly, the condensed water neutralized in the neutralizer tank 103 is the discharge pipe 300 ) through the boiler (not shown).

Upper and lower connecting pipes 100a and 100b that enable the removal and attachment of the neutralizer tank 103 to the outer surface of the diesel pipe 100 in which the inlet pipe 200 and the outlet pipe 300 are integrally communicated as described above According to the formed structure, the neutralizer tank 103 can be selectively installed by removing and attaching the neutralizer tank 103 to the upper and lower connection pipes 100a and 100b according to the acid concentration of the condensate. In this case, the upper and lower connection pipes 100a. 100b are sealed with a sealing stopper 102 , and the condensed water can be discharged through the discharge pipe 300 as it is, and the condensed water that has risen to a predetermined height in the diesel pipe 100 is discharged from the discharge pipe. By discharging it through 300 as it is, the condensed water discharge time can be shortened, and the time for condensed water to stay in the diesel pipe 100 is reduced, so that foreign substances or moss in the diesel pipe 100 or the discharge pipe 300 is prevented from being generated, and by installing a siphon of reduced volume in the boiler, the volume of the boiler is reduced at the same time.

The siphon capable of attaching and detaching a neutralizer tank according to the present invention described above is not limited to the above-described embodiment, and without departing from the gist of the present invention as claimed in the following claims, those of ordinary skill in the art to which the present invention pertains It has the technical spirit to the extent that anyone can change it in various ways.

100: light pipe 100a: upper connection pipe
100b: lower connection pipe 100c: stepped groove part
101: Euro 101a: Upper passage
101b: lower flow passage 102: sealing stopper
103: neutralizer tank 103a: outlet
103b: inlet 103c: connection frame
104: neutralizing agent 105: barrier barrier
200: inlet pipe 300: outlet pipe
400: lower cap 401: protruding wall part
402: through hole

Claims (9)

A light oil pipe 100 having a hollow tubular body shape with an open lower portion, forming a flow path 101 inside, and forming upper and lower connecting pipes 100a and 100b on the outer surface and the lower part;
Inlet pipe ( 200);
a discharge pipe 300 extending integrally with the upper end of the light oil pipe 100 and communicating with the flow path 101 of the light oil pipe 100;
The lower end cap 400 is fixed to the lower end of the light oil pipe 100, sealing the lower portion of the light oil pipe 100;
is composed of
The pass-through pipe 100 is
It has a hollow tubular shape, has a neutralizer 104 therein, and is connected to each of the upper and lower connection pipes 100a and 100b in communication with the flow path 101 on one side and at the bottom 103a) and Further forming a neutralizing agent tank 103 having an inlet 103b,
In the flow path 101 between the gas oil pipe 100 and the inlet pipe 200, it is fitted and fixed to be positioned between the outlet 103a and the inlet 103b of the neutralizer tank 103, the outlet 103a A barrier barrier that blocks the flow path 101 between the inlet and the inlet 103b to block the condensed water in the flow path 101 whose lower portion is closed by the lower cap 400 from moving in the direction of the outlet 103a. (105) is further formed,
The lower cap 400,
The protruding wall portion 401 protruding upwardly between the light oil pipe 100 and the inlet pipe 200 and positioned in the flow path 101, and the protruding wall portion 401 are formed to be spaced apart from each other by a predetermined distance along the outer surface of the , further forming a through hole 402 allowing the condensed water introduced through the inlet pipe 200 to be supplied into the flow path 101 of the light oil pipe 100,
The protrusion wall part 401 allows the blocking partition wall 105 to be fitted and fixed to the upper end thereof, so that the blocking partition wall 105 is a flow path 101 between the upper connection pipe 100a and the lower connection pipe 100b. ), a siphon capable of attaching and detaching the neutralizer tank, characterized in that it is supported so as to be positioned in the position. The method of claim 1,
The pass-through pipe 100 is
The lower end height is formed to be relatively lower than the lower end height of the inlet pipe 200 , so that the condensed water introduced through the inlet pipe 200 is supplied to the flow path 101 of the light oil pipe 100 . Detachable siphon with neutralizer tank. delete delete The method of claim 1,
The flow path 101 of the gas pipe 100 is,
A siphon with detachable neutralizer tank, characterized in that it is divided into upper and lower flow passages (101a, 101b) based on the blocking partition wall (105). The method of claim 1,
The pass-through pipe 100 is
Doedoe recessed along the inner circumferential surface, allowing the blocking partition wall 105 to be caught, preventing the blocking partition wall 105 from flowing up and down between the light oil pipe 100 and the inlet pipe 200 Removable siphon of neutralizer tank, characterized in that it further forms a stepped groove portion (100c). delete The method of claim 1,
The neutralizing agent tank 103,
A connection frame that is fastened to surround the outer surface of the outlet 103a or the inlet 103b and connects the outlet 103a and the upper connector 100a or the inlet 103b and the lower connector 100b ( 103c), the neutralizer tank detachable siphon, characterized in that it is further formed. The method of claim 1,
The discharge pipe 300 is
A siphon capable of attaching and detaching a neutralizer tank, characterized in that it extends integrally from the upper end of the light oil pipe (100) to a downward sloping direction.

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