JP2972884B1 - Neutralization device - Google Patents

Abstract

The present invention provides a compact neutralization device that can neutralize acidic condensed water until it satisfies drainage standards. A treatment tank filled with an alkaline neutralizing agent is provided.
1 and a plurality of partition plates 83 arranged at intervals so as to divide the inside of the treatment layer 81. After neutralizing the acidic condensed water while bending and flowing it in the treatment tank 81, the water is discharged. In the summing device 80, an aluminum 87 that reacts with alkali to generate hydrogen on the downstream side of the treatment layer 81 and a hydrogen sensor 88 that detects the generated hydrogen are provided, and a predetermined amount of hydrogen detected by the hydrogen sensor 88 is provided. When it exceeded, the condensed water was drained from the middle of the treatment layer 81 in a short-circuit manner.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for neutralizing acidic condensed water, and more particularly, to a device for neutralizing acidic condensed water generated by a high-efficiency heat exchanger used for a hot water heater or the like.

[0002]

2. Description of the Related Art When highly efficient heat exchange is performed between a combustion gas generated from a burner or the like and a fluid such as water using a heat exchanger, acidic condensed water in which components in the combustion gas are dissolved. Is generated. If this acidic condensed water is drained as it is,
Drainage pipes and surrounding structures are corroded. Therefore, for example, the neutralizing apparatus disclosed in Japanese Patent Application Laid-Open No. 6-328084 has a configuration in which acidic condensed water is introduced into a retention tank filled with a neutralizing agent, neutralized, and then drained. A general drainage standard defined by the Water Pollution Control Law and prefectural ordinances has a pH of 5.8 or more and 8.6 or less.

[0003]

However, in the above conventional apparatus, the flow path of the condensed water in the neutralizing device is the same regardless of the amount of the condensed water and the aging of the neutralizing agent. In addition, there is a problem that the neutralization condition is not constant and the neutralization performance becomes unstable, for example, the contact time between the neutralizer and the condensed water varies. In addition, when an alkaline neutralizer such as magnesium whose equilibrium PH when reacted with an acid is a strong alkali is used as the neutralizer, the neutralization can be performed with a small amount of the neutralizer, but the condensed water can be used for a long time. If the condensed water and the alkaline neutralizing agent excessively react with each other, the treated water discharged from the neutralizing device becomes alkaline. Further, when the neutralizing agent is filled with a large amount so that the neutralizing agent does not need to be replaced frequently, the treated water immediately after the start of the operation of the neutralizing device also becomes alkaline. SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned conventional problems and to provide a compact neutralizing device that can effectively neutralize condensed water by effectively using a neutralizing agent.

[0004]

In order to achieve the above object, a neutralization apparatus according to the present invention is provided with a treatment tank filled with an alkaline neutralizing agent and a space provided so as to partition the inside of the treatment layer. A plurality of partition plates, and neutralize while bending and flowing the acidic condensed water in the treatment tank, and then, in a neutralization device that drains, reacts with the alkali downstream of the treatment layer to generate hydrogen. Aluminum and a hydrogen sensor for detecting the generated hydrogen are provided, and when hydrogen detected by the hydrogen sensor exceeds a predetermined amount, a first drainage of condensed water from the middle of the treatment layer is performed. Features.

According to the neutralizing device of the first aspect, the acidic condensed water introduced into the neutralizing device and the alkaline neutralizing agent filled in the treatment layer react excessively, and the treated water becomes alkaline. In such a case, the treated water reacts with the aluminum provided on the downstream side of the treated layer to generate hydrogen. Then, when it is detected by the hydrogen sensor that the amount of generated hydrogen exceeds a predetermined amount, the condensed water is discharged in a short-circuit manner in the middle of the treatment layer, so that an excessive reaction is prevented and the water is discharged from the neutralization device. Treated water can always be maintained at a PH that satisfies drainage standards. In addition, the acidic condensed water bends and flows in the treatment layer filled with the alkaline neutralizing agent, so that the contact time with the neutralizing agent is sufficiently ensured and the neutralizing agent is efficiently neutralized with a small amount of the neutralizing agent. And the size of the neutralization device can be reduced. Furthermore, even if the neutralizing agent is filled more than originally required, the treated water can always be maintained at a pH that satisfies the drainage standard. By adjusting the filling amount of the neutralizing agent according to the number of years, it is not necessary to change the neutralizing agent on the way.

Further, in addition to the first feature, the neutralization device of the present invention is characterized in that a plurality of paths for draining condensed water in a short-circuit manner can be switched according to the amount of generated hydrogen. Features.

According to the neutralizing device of the present invention, a plurality of paths for draining condensed water in a short-circuit manner can be switched according to the amount of hydrogen generated. By draining the water upstream of the treatment layer and, when the treated water shows weak alkalinity, draining the water downstream of the treatment layer, the discharged treated water can be adjusted to a pH closer to neutrality.

[0008]

DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is an overall configuration diagram when a neutralization device of the present invention is used for a water heater, and FIG. 2 is a schematic configuration diagram showing an embodiment of the neutralization device of the present invention.

In FIG. 1, a water heater 10 has a main heat exchanger 2 on the upstream side and an auxiliary heat exchanger 4 on the downstream side in the exhaust gas passage 7 above the burner 1 with a drain receiver 6 interposed therebetween. doing. Water supplied from tap water or the like is branched upstream of the main heat exchanger 2 and the auxiliary heat exchanger 4, and is passed through the water pipe 3 and the branch pipe 5. The water passed through the branch pipe 5 is supplied to the auxiliary heat exchanger 4
Then, the water passed through the water pipe 3 joins after being heated by the main heat exchanger 2 respectively, and is discharged from a hot water supply pipe (not shown). That is, the water passed through the branch pipe 5 is heated in the auxiliary heat exchanger 4 by the combustion gas that has been heated by the main heat exchanger 2. At this time, strongly acidic condensed water containing a combustion gas component is generated in the auxiliary heat exchanger 4. The condensed water is supplied to a drain receiver 6 disposed below the auxiliary heat exchanger 4.
After being neutralized by the neutralization device 80, and then drained. The main heat exchanger 2 and the auxiliary heat exchanger 4
Can be adjusted by the flow control valve 9. 110 is a control main body that controls the operation of the water heater 10.

FIG. 2 shows an embodiment of a neutralizing device 80 according to the present invention. In a treatment tank 81, magnesium 82 (equilibrium) is used as an alkaline neutralizing agent whose equilibrium PH when reacted with acid is alkaline. PH = about 10).

The acidic condensed water that has flowed into the treatment layer 81 is bent in the vertical direction while flowing in the tank defined by the partition plate 83 while reacting with the magnesium 82. Magnesium 82
The reaction products and dust generated in the process of neutralizing the acidic condensed water are accumulated in the collection space 85 via the neutralizing agent bottom plate 84 made of perforated metal, wire mesh or the like. .

The treated water neutralized in the treatment layer 81 is drained from the drain pipe 86. Since the magnesium 82 has a high neutralizing capacity per unit volume, even a small amount of the acidic condensed water is relatively short. On the other hand, it is possible to increase the filling amount more than necessary,
When it is brought into contact with 2, the condensed water becomes conversely alkaline due to an excessive neutralization reaction. At this time, the aluminum 87 provided on the downstream side of the treatment layer 81 reacts with the alkaline treatment water to generate hydrogen. The reaction formula is as follows. 2Al + 2OH- + 6H2O → 2Al (OH-) 4 + 3
H2

When the hydrogen sensor 88 detects that the amount of generated hydrogen exceeds a predetermined amount, a signal from the control main unit 110 responds to the amount of generated hydrogen, that is, the intensity of the alkalinity of the treated water. According to the above, either the normally closed solenoid valve 89 or the solenoid valve 90 is opened, and the condensed water is drained in a short-circuit from the middle of the treatment layer 81, so that an excessive reaction is prevented, and The discharged treated water can be constantly maintained at a PH that satisfies the drainage standard.

[0014]

With the above-described configuration, the neutralizing device of the present invention has the following effects. That is, according to the neutralizing device of the first aspect, the acidic condensed water introduced into the neutralizing device and the alkaline neutralizing agent filled in the treatment layer react excessively, and the treated water becomes alkaline. In such a case, the treated water reacts with the aluminum provided on the downstream side of the treated layer to generate hydrogen. Then, when it is detected by the hydrogen sensor that the amount of generated hydrogen exceeds a predetermined amount, the condensed water is discharged in a short-circuit manner in the middle of the treatment layer, so that an excessive reaction is prevented and the water is discharged from the neutralization device. Treated water can always be maintained at a PH that satisfies drainage standards. In addition, the acidic condensed water bends and flows in the treatment layer filled with the alkaline neutralizing agent, so that the contact time with the neutralizing agent is sufficiently ensured and the neutralizing agent is efficiently neutralized with a small amount of the neutralizing agent. And the size of the neutralization device can be reduced. Furthermore, even if the neutralizing agent is filled more than originally required, the treated water can always be maintained at a pH that satisfies the drainage standard. By adjusting the filling amount of the neutralizing agent according to the number of years, it is not necessary to change the neutralizing agent on the way. According to the neutralization device of claim 2, a plurality of paths for draining condensed water in a short-circuit manner can be switched according to the amount of generated hydrogen. When the treated water shows weak alkalinity and is discharged on the downstream side in the treatment layer, the discharged treated water can be adjusted to a pH closer to neutrality.

[Brief description of the drawings]

FIG. 1 is an overall configuration diagram of a water heater using a neutralization device of the present invention.

FIG. 2 is a sectional view of a main part showing an embodiment of a neutralization device of the present invention.

[Explanation of symbols]

 2 Main heat exchanger 4 Auxiliary heat exchanger 80 Neutralizer 81 Treatment layer 82 Magnesium 83 Partition plate 86 Drainage pipe 87 Aluminum 88 Hydrogen sensor 89 Solenoid valve 90 Solenoid valve

──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. ⁶ Identification code FI F24H 9/00 F24H 9/00

Claims (2)

(57) [Claims] 1. A treatment tank filled with an alkaline neutralizing agent,
A plurality of partition plates arranged at intervals so as to partition the inside of the treatment layer, and neutralized while making acidic condensed water bend and flow in the treatment tank, and then drained, the neutralization device to drain, An aluminum that generates hydrogen by reacting with alkali on the downstream side of the processing layer and a hydrogen sensor that detects the generated hydrogen are provided.When the amount of hydrogen detected by the hydrogen sensor exceeds a predetermined amount, the processing layer A neutralization device characterized in that condensed water is drained from the middle in a short-circuit manner. 2. The neutralization device according to claim 1, wherein a plurality of paths for draining condensed water in a short-circuit manner can be switched according to the amount of generated hydrogen.