JP2005288219A - Water supply system - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a water supply system which can suppress corrosion due to lowering of pH of water supplied into equipment such as thermal equipment and water treatment equipment. <P>SOLUTION: The water supply system 3 for supplying water to a boiler 2 as thermal equipment is constituted by providing a water supply line 4 for making supply water flow, a straining treatment section 8 which is installed in the water supply line 4 and which performs straining treatment with a filtering member for catching corrosion propagating components causing corrosion of the boiler 2, a bypass line 10 which makes water flow through the water supply line 4 at an upstream side of the straining treatment section 8 bypass to the water supply line 4 at a downstream side of the straining treatment section 8, a stop valve 11 installed in the bypass line 10 and a controlling section 14 which controls opening/closing of the stop valve 11 so that water flowing at the downstream side of the straining treatment section 8 and supplied to the boiler 2 has predetermined M alkalinity. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to a water supply system for supplying treated water generated by reforming raw water to equipment such as heat equipment and water treatment equipment as feed water.

  For example, in the heat equipment such as a steam boiler, a hot water boiler, a cooling tower, and a water heater, treated water obtained by removing impurities and / or dissolved gas from raw water is used.

Conventionally, as a water supply system for supplying treated water generated by reforming the raw water to a thermal device, generally, impurities and the like contained in the raw water are filtered by a reverse osmosis membrane portion using a reverse osmosis membrane, Next, what dissolve | melts the dissolved gas in raw | natural water by a deaeration process part and modify | reforms it to the water quality suitable for use with an apparatus is known (for example, refer patent document 1).
Japanese Patent Laid-Open No. 5-220480

  However, according to the water supply system, the reverse osmosis membrane also captures alkaline components contained in the raw water. Thus, when the water supply from which the alkaline component was removed is supplied to the heat equipment, the pH of the water supply in the heat equipment does not increase, which may promote corrosion of the heat equipment. In such a case, since the water supply before passing through the filtration treatment unit contains an alkali component, it is particularly suitable when the quality of the treated water after the filtration treatment by the reverse osmosis membrane unit has a margin. Therefore, it is conceivable to effectively use the water supply before passing through the reverse osmosis membrane portion.

  The objective of this invention is providing the water supply system which can suppress the corrosion by the fall of pH of the feed water supplied to apparatuses, such as a thermal apparatus and a water treatment apparatus.

  In order to solve the above-mentioned problem, the invention described in claim 1 is a water supply system for supplying water to equipment, wherein a water supply line for flowing the water supply, and a filtration processing unit provided in the water supply line, , A bypass line for bypassing the filtration processing unit, an on-off valve provided on the bypass line, and a control for opening / closing the on-off valve so that water supplied downstream of the filtration processing unit has a predetermined M alkalinity And a portion.

  In the water supply system according to the first aspect of the present invention, the feed water flowing through the feed water line is supplied to the filtration processing unit, and the filtration processing unit removes impurities contained in the supplied feed water.

  When the M alkalinity of the feed water from which impurities have been removed, that is, the feed water supplied to the flow equipment downstream of the filtration processing unit is low, the control unit opens the on-off valve and flows into the filtration processing unit. The previous water supply is allowed to flow from the bypass line to the downstream side of the filtration unit. When the water supply reaches a predetermined M alkalinity, the control unit closes the on-off valve.

  The invention described in claim 2 is characterized in that a degassing processing section is provided in the water supply line on the downstream side of the filtration processing section described in claim 1.

  In such a water supply system according to the second aspect of the invention, the dissolved gas contained in the permeated water that has permeated through the filtration unit is removed. Thereby, the treated water from which impurities and dissolved gas are removed is generated.

  According to a third aspect of the present invention, the bypass line according to the second aspect connects a water supply line on the upstream side of the filtration processing unit and a water supply line between the filtration processing unit and the deaeration processing unit. It is characterized by having comprised as follows.

  In such a water supply system according to the third aspect of the present invention, the water supply bypassed from the upstream side to the downstream side of the filtration processing unit is supplied to the equipment through the deaeration processing unit.

  According to the first aspect of the present invention, filtration is performed by an alkaline component such as bicarbonate, carbonate, hydroxide, etc. contained in the water supply upstream of the filtration unit that flows into the downstream side of the filtration unit. The M alkalinity of the feed water supplied to the flow equipment on the downstream side of the processing unit can be increased. Thereby, the fall of pH of the feed water supplied in the apparatus can be prevented, and corrosion of an apparatus can be suppressed effectively.

  According to invention of Claim 2, since the dissolved gas in the feed water supplied to an apparatus is removed, the corrosion inhibitory effect of an apparatus can be improved.

  According to invention of Claim 3, since the dissolved gas contained in the feed water bypassed from the upstream of the filtration process part is removed by the said deaeration process part, the corrosion inhibitory effect of an apparatus is improved. be able to.

Hereinafter, the best mode for carrying out the water supply system according to the present invention will be described.
(Embodiment 1)
The water supply system of this example is a water supply system for supplying water to equipment, and includes a water supply line through which the water supply flows, a filtration processing unit provided in the water supply line, and a bypass line that bypasses the filtration processing unit And an opening / closing valve provided in the bypass line, and a control unit that controls the opening / closing of the opening / closing valve so that water supplied downstream of the filtration processing unit has a predetermined M alkalinity. It is a feature.

  The said filtration process part removes the impurity contained in the water supply which flows through the said water supply line with a filter membrane. Examples of filtration membranes include nanofiltration membranes and RO membranes. Impurities removed by such a filtration membrane also include alkali components such as bicarbonates, carbonates and hydroxides.

  When the permeated water from which impurities such as alkali components have been removed, that is, when the M alkalinity of the feed water supplied to the flow equipment on the downstream side of the filtration processing unit is low, it is opened and closed by the control unit. The valve is opened, and the feed water before flowing into the filtration processing unit is caused to flow from the bypass line to the downstream side of the filtration processing unit. The alkalinity component contained in the feed water flowing in from the bypass line can increase the M alkalinity of the feed water supplied to the flow equipment downstream of the filtration unit. Thereby, the fall of pH of the feed water supplied in the apparatus can be prevented, and corrosion of an apparatus can be suppressed effectively.

(Embodiment 2)
The water supply system of this example is a water supply system for supplying water to equipment, and includes a water supply line through which the water supply flows, a filtration processing unit provided in the water supply line, and the downstream of the filtration processing unit. A deaeration unit provided in the water supply line; a bypass line that bypasses the filtration unit and connects a water line on the upstream side of the filtration unit and a water line between the filtration unit and the deaeration unit; And an opening / closing valve provided in the bypass line, and a control unit that controls opening / closing of the opening / closing valve so that water supplied downstream of the filtration processing unit has a predetermined M alkalinity. It is said.

  In such a water supply system of this example, in the filtration processing unit, the filtration membrane removes impurities contained in the feed water flowing through the feed water line, and the degassing processing unit removes dissolved gas in the feed water. Do. Examples of the filtration membrane include nanofiltration membranes and RO membranes as in the first embodiment.

  When the permeated water from which impurities such as alkali components have been removed, that is, when the M alkalinity of the feed water supplied to the flow equipment on the downstream side of the filtration processing unit is low, the control unit opens the on-off valve. The feed water before flowing into the filtration processing unit is caused to flow from the bypass line to the feed water line between the filtration processing unit and the deaeration processing unit. The alkalinity component contained in the feed water flowing in from the bypass line can increase the M alkalinity of the feed water supplied to the flow equipment downstream of the filtration unit. Further, the feed water flowing from the bypass line and the permeated water that has passed through the filtration processing unit are deaerated by the deaeration processing unit, and the dissolved gas is removed. Thereby, since the fall of pH of the feed water supplied in the apparatus can be prevented, and also dissolved gas can be removed, corrosion of an apparatus can be suppressed effectively.

Next, specific embodiments of the present invention will be described in detail with reference to the drawings. In the examples described below, the equipment is a boiler, and the filtration processing unit is a filtration processing unit using a nanofiltration membrane.
First, a first embodiment of the present invention will be described. FIG. 1 is a block diagram showing a first embodiment of a boiler system including a water supply system of the present invention.

  In the figure, a boiler system denoted by reference numeral 1 includes a boiler 2 that heats feed water to generate steam, and a feed water system 3 that supplies feed water to the boiler 2. The water supply system 3 includes a water supply line 4, and treated water generated by reforming the quality of the water supply water on the water supply line 4 is supplied to the boiler 2 as the water supply.

  The boiler 2 is a multi-tube type once-through boiler called a water tube boiler, and this boiler 2 is not particularly shown, but includes an annular lower header and an annular upper header arranged vertically at predetermined intervals. , A plurality of heat transfer tubes disposed between them, a combustion chamber defined by the plurality of heat transfer tubes, and a burner disposed above the combustion chamber and generating steam by heating the feed water in each heat transfer tube It is the boiler of the well-known structure comprised including heating apparatuses, such as. The water supply line 4 is connected to the lower header of the boiler 2.

  The plurality of heat transfer tubes and the like are formed using a non-passivated metal. Here, the non-passivated metal will be described. The non-passivated metal refers to a metal that does not passivate naturally in a neutral aqueous solution. Usually, stainless steel, titanium, aluminum, chromium, nickel, And metals other than zirconium and the like. Specifically, carbon steel, cast iron, copper, copper alloy, and the like. The carbon steel may be passivated in the presence of a high concentration of chromate ions even in a neutral aqueous solution, but this passivation is due to the effects of chromate ions. It ’s hard to say that it ’s a natural passivation. Carbon steel therefore belongs to the category of non-passivated metals here. In addition, copper and copper alloys are considered to be metals that are unlikely to corrode due to the influence of moisture because of the noble position of the electrochemical series (emf series), but they are naturally passive in neutral aqueous solutions. It belongs to the category of non-passivated metals here.

  The water supply system 3 is supplied with water from a raw water tank (not shown) in which raw water supplied from water sources such as tap water, industrial water, and groundwater is stored. Then, the water supply system 3 moves the activated carbon filtration processing unit 5, the water softening processing unit 6, the prefilter 7, the filtration processing unit 8, and the water supply tank 9 to the water supply line 4 from the upstream side toward the downstream side. In order. Further, the water supply system 3 is provided with a bypass line 10 that connects the water supply line 4 between the water softening processing unit 6 and the pre-filter 7 and the water supply tank 9, and the bypass line 10 has an on-off valve 11. Is provided.

  The activated carbon filtration unit 5 is configured as an apparatus for adsorbing and removing an oxidizing agent such as sodium hypochlorite dissolved in the water supply. The oxidizing agent, that is, residual chlorine may oxidize the ion exchange resin (not shown) of the water softening treatment unit 6 disposed on the downstream side of the activated carbon filtration treatment unit 5 to deteriorate the ion exchange capability at an early stage. Moreover, there is a possibility that the nanofiltration membrane (not shown), which will be described later, of the filtration processing unit 8 arranged further downstream is oxidized to deteriorate the filtration capability at an early stage. Therefore, in order to prevent such early deterioration of capacity due to oxidation, the residual chlorine is adsorbed and removed by activated carbon, thereby preventing the early deterioration of the ion exchange capacity and the early deterioration of the filtering capacity. In addition, the water treatment efficiency is improved and stabilized.

  Other devices for removing residual chlorine in the water supply, such as the activated carbon filtration processing unit 5, include a chemical injection device that adds sodium bisulfite (SBS), although not particularly shown, and this is the activated carbon filtration processing unit 5. It may be applied instead of.

  The water softening treatment unit 6 is configured as a device that removes hardness components such as calcium and magnesium contained in the water supply from which the residual chlorine has been removed by using an ion exchange resin (not shown). That is, the water softening process part 6 is comprised as an apparatus for replacing various hardness components contained in water supply with sodium ion, and converting water supply into soft water.

  The pre-filter 7 is configured to prevent the clogging or the like of the filtration member (not shown) of the filtration processing unit from being clogged with dust or the like in the feed water. Etc. are removed in front of the filtration unit 8.

  The filtration processing unit 8 includes a filtration member (not shown) that captures a corrosion promoting component that causes corrosion of the non-passivated metal of the boiler and transmits the corrosion inhibiting component that contributes to the inhibition of the corrosion. It is comprised as what feeds water by a member.

  Specifically, the filtration member is a nanofiltration membrane (NF membrane, NF: Nanofiltration) in this example. This nanofiltration membrane is a synthetic polymer membrane such as polyamide-based or polyether-based, and is a liquid separation membrane that can prevent permeation of particles and polymers (molecular weight of about several hundreds at the maximum) smaller than about 2 nm. In addition, the nanofiltration membrane can be separated from a membrane having a molecular weight of about 1,000 to 300,000 (UF membrane) and a membrane having a molecular weight of about several tens in terms of filtration function. It is a liquid separation membrane having a function located in the middle of the membrane (RO membrane). Incidentally, nanofiltration membranes are commercially available from various companies and can be easily obtained.

Such a nanofiltration membrane captures corrosion promoting components. Here, the corrosion promoting component will be described. The corrosion promoting component means that moisture (here, canned water) adheres to the portion of the boiler 2 where corrosion of the heat transfer tubes (not shown) is likely to occur, particularly inside. , And the one that acts on the inner surface of each heat transfer tube (not shown) that is heated from the outside and promotes its corrosion. Usually, sulfate ions (SO ₄ ²⁻ ), chloride ions (Cl ⁻ ), and others Contains ingredients. Incidentally, both sulfate ions and chloride ions are important as corrosion promoting components. By the way, Japanese Industrial Standard JIS B 8223: 1999 specifies various management items and recommended standards regarding the water quality of the boiler water from the viewpoint of suppressing the corrosion of the special circulation boiler including the once-through boiler. In the regulations, the regulation value of chloride ion concentration is set, but it does not mention the sulfate ion concentration in canned water (in other words, it is recognized that sulfate ions are involved in corrosion). Absent). However, as a result of researches on the relationship between water quality and corrosion of can water over many years, the researchers of the applicant's company have found that each of the above heat transfer tubes (not shown) is sulfate ions contained in can water as a corrosion promoting component. It has been confirmed that it is acting on etc.

  The nanofiltration membrane also captures alkali components such as bicarbonate, carbonate, hydroxide.

And the said nanofiltration membrane permeate | transmits the corrosion inhibitory component which is a component which suppresses corrosion. The corrosion inhibiting component is a part that acts on the inner surface of each heat transfer tube (not shown) of the boiler 2 where corrosion of the heat transfer tube (not shown) is likely to occur, and can suppress the corrosion generated there. That is, it usually contains silica (ie, silicon dioxide (SiO ₂ )). This silica is a component usually contained in tap water, industrial water, groundwater, etc. used as water supply, and is usually recognized as a scale generating component in each heat transfer tube (not shown), and is usually as much as possible. It is considered preferable to suppress the concentration. However, as a result of researches on the relationship between water quality and corrosion of can water over many years, the researchers of the applicant's company have made silica contained in can water as a corrosion-inhibiting component, and the above heat transfer tubes (not shown), etc. It is confirmed that it is acting on.

  The water supply tank 9 provided on the downstream side of the filtration treatment unit 8 is softened by the water softening treatment unit 6, and the corrosion treatment component and the alkali component are captured in the filtration treatment unit 8, and the corrosion inhibition component is permeated. The generated treated water flows from the water supply line 4.

  The water supply tank 9 is provided with an electric conductivity meter 12 as a water quality detection means. The electrical conductivity measured by the electrical conductivity meter 12 is input to the control unit 14 as a water quality detection signal via the signal line 13. Based on the electrical conductivity measured by the electrical conductivity meter 12, the control unit 14 opens and closes the on-off valve 11 via the signal line 15 so as to optimize the M alkalinity in the water supply tank 9. (Bypass operation described later).

  Next, the flow during operation of the boiler 2 will be described based on the above configuration. When the boiler 2 is operated, it is necessary to reform the quality of feed water supplied from a raw water tank (not shown) to generate treated water, and to store the treated water in the feed water tank 9 as feed water for the boiler 2. . The process up to this point will be described. Water supplied through the water supply line 4 flows out from a raw water tank (not shown) at a predetermined pressure by a water supply pump (not shown) having a predetermined discharge pressure. The pressure of the water supply flowing out is set in consideration of pressure loss and the like in each part of the activated carbon filtration processing unit 5, the water softening processing unit 6, the prefilter 7, and the filtration processing unit 8 arranged on the downstream side. And the feed water which flowed out from the raw | natural water tank which is not illustrated first passes the activated carbon filtration process part 5, and will be in the state from which the residual chlorine was removed. Next, the water supply passes through the water softening treatment unit 6 and becomes soft water. Subsequently, when the water supply, which is soft water, passes through the nanofiltration membrane in the filtration unit 8, corrosion promoting components such as sulfate ions and chloride ions, and bicarbonates, carbonates, hydroxides, etc. The alkali component is captured by the nanofiltration membrane. That is, the corrosion promoting component and the alkali component are removed from the soft water. On the other hand, silica contained in the soft water, that is, the corrosion inhibiting component permeates the nanofiltration membrane together with the soft water. The filtered soft water that has been filtered in this way is stored in the water supply tank 9 as water supplied to the boiler 2.

  The treated water (water supply) stored in the water supply tank 9 is supplied to the boiler 2 via a water supply pump (not shown) disposed between the water supply tank 9 and the boiler 2 and stored as can water in the lower header. The The stored can water rises in each heat transfer tube while being heated by the heating device, and gradually becomes steam. And the steam produced | generated in each heat exchanger tube is collected in an upper header, and is supplied to a load apparatus.

  By the way, during the operation of the boiler 2, each heat transfer tube has its lower end portion, that is, the connection portion with the lower header, continuously in contact with the can water. Therefore, each heat transfer tube is likely to corrode under the influence of can water at the lower end portion. In particular, each heat transfer tube is liable to cause local corrosion in addition to thinning corrosion on the inner peripheral surface at the lower end portion, and may cause breakage due to minute holes.

  The above-mentioned local corrosion is a hole-shaped corrosion from the contact surface side of each heat transfer tube with the can water toward the opposite side of the thickness direction, that is, a hole shape generated in the thickness (thickness) direction of each heat transfer tube. Say no corrosion. Hereinafter, such a local corrosion occurrence phenomenon is referred to as “pitting corrosion”, and pitting corrosion caused by this pitting corrosion is referred to as “corrosion”. Incidentally, it is understood that pitting corrosion usually occurs due to the influence of dissolved oxygen in the can water.

  However, according to this example, during operation of the boiler 2, soft water containing a corrosion inhibiting component is supplied to each heat transfer tube as canned water, so that the corrosion inhibiting component contained in the canned water is transferred to each heat transfer tube. It acts on the lower end portion of the heat pipe and suppresses corrosion of the portion. More specifically, the corrosion-inhibiting component suppresses thinning corrosion at the contact portion of each heat transfer tube with the can water, and also suppresses the generation and growth of pits. Suppresses damage to heat tubes. At this time, since the corrosion promoting component is removed from the can water by the filtration processing unit 8, the above-described corrosion inhibiting action by the corrosion inhibiting component is hardly inhibited by the corrosion promoting component and is effectively exhibited. Become.

  Now, corrosion of each heat transfer tube is suppressed by the corrosion-inhibiting component contained in the can water, and it is eluted from each heat transfer tube due to the influence of dissolved oxygen, etc. (corrosion promoting component of each heat transfer tube) contained in the can water This is probably because a corrosion-inhibiting component (particularly silica) acts on the component to form a corrosion-resistant film (corrosion-resistant film) on the inner surface of each heat transfer tube. In particular, dissolved oxygen may cause a local anode to appear in each heat transfer tube, thereby causing pitting corrosion, but the corrosion inhibiting component (silica) contained in the can water is an anion or a negatively charged micelle. Since it exists, it is easy to adsorb | suck to the above anodes and it is easy to selectively form an anticorrosion film in the said part. Therefore, it is considered that the corrosion inhibiting component (silica) contained in the can water can effectively suppress the progress of pitting corrosion in each heat transfer tube.

  In the filtration processing unit 8, an alkaline component in the feed water is captured by the nanofiltration membrane. Therefore, there is a possibility that the pH of the can water in the heat transfer tubes may not increase, particularly in an area where the water quality is low with less alkaline components in the feed water. When the pH of the can water in the heat transfer tube is lower than a predetermined value, the heat transfer tube is easily corroded. Therefore, when it is detected that the M alkalinity in the feed water is lower than a predetermined value based on the electrical conductivity of the treated water in the feed water tank 8, the on-off valve 11 is opened and closed, thereby flowing into the filtration processing unit 8. A bypass operation for bypassing the previous water supply from the bypass line 10 is performed.

  The bypass operation will be described in detail. The electrical conductivity in the water supply tank 9 measured by the electrical conductivity meter 12 is input to the control unit 14 as a water quality detection signal via the signal line 13. Upon receiving the water quality detection signal, the control unit 14 opens and closes the on-off valve 11 and performs feedback control so that the M alkalinity of the treated water in the water supply tank 9 is optimized. That is, the water quality detection signal detected by the electrical conductivity meter 12 is input to the control unit 14 via the signal line 13, and the control unit 14 determines that the input electrical conductivity is smaller than a predetermined value. The on-off valve 11 is opened. Thereby, the water supply before being filtered by the filtration processing unit 8 flows into the water supply tank 9 from the bypass line 10. Since the alkaline component is not captured by the filtration processing unit 8 in this water supply, the M alkalinity in the water supply tank 9 into which the water supply has flowed increases. Then, the control unit 14 closes the on-off valve 11 when determining that the predetermined electrical conductivity has been reached based on the water quality detection signal from the electrical conductivity meter 12.

  As described above, the nanofiltration that captures the corrosion promoting component that causes the corrosion of the non-passivated metal body of the boiler 2 in the water supply line 4 of the boiler system 1 and permeates the corrosion inhibiting component that contributes to the suppression of the corrosion. By providing the filtration processing unit 8 that performs filtration using a membrane, corrosion that occurs in the heat transfer tube of the boiler 2 can be suppressed without using any chemicals.

  Further, when the electrical conductivity of the treated water in the water supply tank 9 becomes smaller than a predetermined value, the on-off valve 11 is opened to supply the water in a state where the alkali component before passing through the filtration processing unit 8 is not captured. Since it flows into the water supply tank 9 from the bypass line 10, the M alkalinity of the treated water in the water supply tank 9 can be raised, and the fall of the pH of can water can be prevented.

  In the said Example, although the position which bypasses the water supply of the upstream of the filtration process part 8 by the bypass line 10 is the water supply tank 9, it is not restricted to such a case, For example, the filtration process part 8 And the water supply line 4 between the water supply tank 9 and the water supply tank 9 may be bypassed.

  Next, a second embodiment of the present invention will be described with reference to FIG. FIG. 2 is a block diagram showing a second embodiment of the boiler system including the water supply system of the present invention. In the following description, the same components as those in the first embodiment are denoted by the same reference numerals and description thereof is omitted.

  The water supply system 20 of this example includes a deaeration processing unit 21 between the filtration processing unit 8 and the water supply tank 9. And the bypass line 10 is comprised so that the water supply line 4 between the water softening process part 6 and the pre filter 7 and the water supply line 4 between the filtration process part 8 and the deaeration process part 21 may be connected, and a filtration process is carried out. The water supply before being filtered in the unit 8 is bypassed downstream of the filtering unit 8 and before the deaeration unit 21.

  The deaeration unit 21 mechanically removes the dissolved oxygen contained in the permeated water filtered by the filtration unit 8 and the feed water flowing from the bypass line 10. The deaeration processing unit 9 includes a deaeration membrane (not shown), and circulates the permeate through one of the deaeration membranes, and sucks the other with a vacuum exhaust means such as a vacuum pump. It has a well-known configuration for degassing dissolved oxygen.

  In such a water supply system 20 of this example, water supplied from a raw water tank (not shown) passes through the activated carbon filtration processing unit 5, the water softening processing unit 6, the prefilter 7, and the filtration processing unit 8, thereby Similar to the embodiment, the water becomes soft water, the corrosion promoting component is captured and the corrosion inhibiting component permeates, and this water supply is supplied to the deaeration treatment unit 21 to deaerate dissolved oxygen. Treated water that is soft water containing the corrosion inhibiting component after the deaeration treatment is stored in the feed water tank 9 as feed water supplied to the boiler 2.

  In this example, the water supply which flows through the water supply line 4 between the water softening process part 6 and the pre filter 7 by opening the on-off valve 11 based on the electrical conductivity in the water supply tank 9 measured with the electric conductivity meter 12. However, it flows into the water supply line 4 between the filtration processing unit 8 and the deaeration processing unit 21 through the bypass line 10. Thereby, the M alkalinity in the water supply tank 9 can be raised like the said 1st Example.

  According to the water supply system 20 of the present example described above, the corrosion promoting component is captured and the water supply through which the corrosion inhibiting component is transmitted is supplied to the boiler 2, so that the corrosion that occurs in the heat transfer tube of the boiler 2 is not used. In addition, it is possible to prevent the pH of the can water from being lowered. Moreover, the dissolved oxygen dissolved in the permeated water filtered by the filtration processing unit 8 and the feed water from the bypass line 10 is removed in the degassing processing unit 21, and the corrosion inhibition effect can be improved.

The block diagram which shows 1st Example of the boiler system containing the water supply system of this invention. The block diagram which shows 2nd Example of the boiler system containing the water supply system of this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Boiler system 2 Boiler 3,20 Water supply system 4 Water supply line 5 Activated carbon filtration part 6 Soft water treatment part 7 Prefilter 8 Filtration part 9 Water supply tank 10 Bypass line 11 On-off valve 12 Conductivity meter 13 Signal line 14 Control part 15 Signal line 21 Deaeration processing part

Claims (3)

A water supply system for supplying water to equipment,
A water supply line for flowing the water supply;
A filtration unit provided in the water supply line;
A bypass line that bypasses the filtration unit;
An on-off valve provided in the bypass line;
A control unit that controls opening and closing of the on-off valve so that water supply flowing downstream of the filtration unit has a predetermined M alkalinity;
The water supply system characterized by comprising. The water supply system according to claim 1, wherein a deaeration processing unit is provided in the water supply line on the downstream side of the filtration processing unit. The water supply system according to claim 2, wherein the bypass line is configured to connect a water supply line upstream of the filtration processing unit and a water supply line between the filtration processing unit and the deaeration processing unit. system.

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