Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP4600680B2 - Water supply system - Google Patents
[go: Go Back, main page]

JP4600680B2 - Water supply system - Google Patents

Water supply system Download PDF

Info

Publication number
JP4600680B2
JP4600680B2 JP2006037198A JP2006037198A JP4600680B2 JP 4600680 B2 JP4600680 B2 JP 4600680B2 JP 2006037198 A JP2006037198 A JP 2006037198A JP 2006037198 A JP2006037198 A JP 2006037198A JP 4600680 B2 JP4600680 B2 JP 4600680B2
Authority
JP
Japan
Prior art keywords
water
tank
groundwater
pipe
treated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP2006037198A
Other languages
Japanese (ja)
Other versions
JP2007192004A (en
Inventor
翼 勝田
教雄 野村
孝悦 福田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Aqua Solutions Co Ltd
Original Assignee
Wellthy Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wellthy Corp filed Critical Wellthy Corp
Priority to JP2006037198A priority Critical patent/JP4600680B2/en
Publication of JP2007192004A publication Critical patent/JP2007192004A/en
Application granted granted Critical
Publication of JP4600680B2 publication Critical patent/JP4600680B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/10Geothermal energy

Landscapes

  • Sorption Type Refrigeration Machines (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Description

本発明は、年間を通じ水温の変化の少なく、有効恒温性を活用可能な地下水を対象とするもので、代表例で説明すると、深度100m以深に滞留している地下水を揚水し、濾過処理をする事により、活用目的にあった水質を具現するシステムに関する。
例えば、当該地下水の恒温性、水質の清廉さを活用する事により、併せて公害防止、省資源、省エネルギー、炭酸ガス等の抑制に益するべく追及するものである。
The present invention is intended for groundwater that has little change in water temperature throughout the year and is capable of utilizing effective isothermal properties. In a typical example, groundwater staying at a depth of 100 m or more is pumped and filtered. It relates to a system that realizes the water quality suitable for the purpose of use.
For example, by utilizing the constant temperature and water quality of the groundwater, we will pursue the benefits to prevent pollution, save resources, save energy, and control carbon dioxide.

従来、水冷空調機とりわけ多く利用されている冷温水発生器等の凝縮器冷却方式として、冷却塔による循環冷却水方式が多く採用されている。確かに、循環方式を採用するために補給水の供給のみとする点で水資源の有効活用に優れるが、冷却水温度はレジオネラ属菌の増殖帯にあり基本的な問題点を抱えている。
即ち、冷却塔を介して大気に噴霧状の水滴(エアロゾル)がレジオネラ属菌を含む状態で放散され、感染症を引き起こす危険を多く孕んでいるのが現状である。この対策として、冷却水に薬剤注入、磁力線照射による殺菌、オゾン殺菌等によりレジオネラ属菌類撲滅対策が実行されている。
Conventionally, a circulating cooling water system using a cooling tower is often employed as a cooling system for a water-cooled air conditioner, particularly a cooling / hot water generator that is widely used. Certainly, it is excellent in the effective use of water resources in that only the supply of makeup water is used to adopt the circulation method, but the cooling water temperature is in the growth zone of Legionella spp. And has a basic problem.
That is, under the present circumstances, sprayed water droplets (aerosol) are diffused into the atmosphere through the cooling tower in a state containing Legionella spp., And there is a great risk of causing infections. As countermeasures, Legionella genus eradication measures are implemented by injecting chemicals into cooling water, sterilization by irradiation of magnetic field lines, ozone sterilization, and the like.

ところが、レジオネラ属菌類の発育最適温度は36℃前後で、これらの菌類は藻類その他の細菌類の代謝産物を利用するか或いは原生動物に寄生して増殖するもので、撲滅にはこれらの微生物類との共生関係を遮絶する事が重要と認識する。
即ち、レジオネラ属菌類は冷却水中の様々な環境条件下生息し、その冷却水を大気中に放散する事により濃縮を起こし、特に夏季には水温の上昇による藻類や原生動物の発生が加速され更に増殖に適した環境に移行する。
以上の通り、温度、微生物共生、濃縮の条件に基づき冷却水中でのレジオネラ属菌類の発生、増殖が左右されるものと考えられている。
However, the optimal growth temperature of Legionella spp. Is around 36 ° C., and these fungi use the metabolites of algae and other bacteria or infest with protozoa. Recognize that it is important to block the symbiotic relationship.
In other words, Legionella spp. Live in various environmental conditions in cooling water and cause concentration by releasing the cooling water into the atmosphere. Especially in summer, the generation of algae and protozoa due to rising water temperature is accelerated. Move to an environment suitable for growth.
As described above, it is considered that the generation and growth of Legionella spp. In cooling water are influenced by temperature, microbial symbiosis, and concentration conditions.

レジオネラ属菌類の発育至適温度は36℃前後であるが、25〜43℃の範囲内で十分に生育出来、凍結下の−80℃でも死滅しない。特に、冷却塔水中のレジオネラ属菌類は4〜5℃で年間を通じ生存し、低温では増殖しないものの環境が適温に変化し次第増殖に転じる。
又、70℃の湯に直接接触すれば5秒以内に、60℃の湯または0.4ppmの遊離残留塩素に接触すれば15分以内に死滅する。一方、レジオネラ属菌類そのものは清浄な水中では紫外線で殺菌出来るが、その後可視光線を受け光回復するとされている。
The optimum temperature for the growth of Legionella spp. Is around 36 ° C., but it can grow sufficiently within the range of 25-43 ° C. and does not die even at −80 ° C. under freezing. In particular, Legionella spp. In the cooling tower water survive throughout the year at 4 to 5 ° C., but do not grow at low temperatures, but the environment changes to an appropriate temperature and begins to grow.
Moreover, it will die within 5 seconds if it comes into direct contact with 70 ° C. hot water, and within 15 minutes if it comes into contact with 60 ° C. hot water or 0.4 ppm free residual chlorine. On the other hand, Legionella spp. Itself can be sterilized with ultraviolet light in clean water, but it is said to recover by receiving visible light thereafter.

以上の報告からも現状ではレジオネラ属菌類の撲滅は非常に困難で、何時どこで感染症が発症しても不思議でない状況を潜在的に抱えている。
そこで、根本的対策ではレジオネラ属菌類自体の生息、増殖を根幹より阻止出来る環境を創出する以外に抜本的適策は無いものと想定される。行政においても感染症防止対策の指針を発表しているものの現状では依然として危険回避は不十分である。
この様な状況を脱却するには、問題の原点とされる冷却方式の改善が望まれており、冷却手段として地表面下に存在する天然の恒温性の活用に着目されている。
例えば、地下の空気及び地下水の温度利用による冷暖房システム(例えば、特許文献1参照)や、年間を通じて一定温度の地下水を直接利用した冷暖房装置(特許文献2参照)や、一般家庭等の飲料水、その他の生活雑水、冷暖房等に地下水を最大限に利用した住宅トータルシステムの提供(特許文献3参照)等が報告されている。
From the above reports, it is very difficult to eradicate Legionella spp., And there is a potential situation where no matter where and when an infection develops.
Therefore, it is assumed that there are no radical measures other than creating an environment that can prevent the Legionella spp. Although the government has announced guidelines for measures to prevent infectious diseases, at present, risk aversion is still insufficient.
In order to escape from such a situation, improvement of the cooling system, which is the starting point of the problem, is desired, and attention is paid to the use of natural thermostatic properties existing below the ground surface as a cooling means.
For example, a cooling / heating system using the temperature of underground air and groundwater (for example, see Patent Document 1), a cooling / heating device (see Patent Document 2) that directly uses groundwater at a constant temperature throughout the year, drinking water for general households, There have been reports of provision of a total housing system (see Patent Document 3) that uses groundwater to the maximum extent for other domestic miscellaneous water and air conditioning.

特開2003−247731  JP 2003-247731 A 特開2003−90630  JP 2003-90630 A 特開2002−146852  JP2002-146852

この様な観点に立ち、現状の冷却塔による冷却水循環方式ではレジオネラ属菌の発生、増殖は避けられないとの認識から、様々な対応策を考案されているものの、未だ撲滅には至らない現状である。
本発明者等は、省エネ、省資源の目標に自然界に存在する地下の恒温環境の活用を手段に取り入れ、従来の冷却塔方式より直接冷却方式に切り替え、レジオネラ属菌類の発生経路の遮断と水資源の有効活用の両面で、所期の目的を達成することを目指した。
この結果、レジオネラ属菌類の空中放散の制止と、地下の恒温環境効果が地下水を熱交換の媒体として有効活用する事により達成出来る事を課題とした。
From this perspective, various countermeasures have been devised based on the recognition that the generation and growth of Legionella spp. Is inevitable with the current cooling water circulation system using a cooling tower, but it has not yet been eradicated. It is.
The inventors of the present invention have taken into account the utilization of the underground constant temperature environment that exists in nature as a means of energy and resource saving, switched from the conventional cooling tower method to the direct cooling method, blocking the path of generation of Legionella and water The aim was to achieve the intended objectives in terms of effective use of resources.
As a result, it was an issue that the suppression of Legionella spp. In the air and that the effect of the subsurface isothermal environment could be achieved by effectively using the groundwater as a heat exchange medium.

レジオネラ属菌類の撲滅対策を念頭に、地下の恒温性を直接反映する媒体として地下水の有効介在を中心に、従来の冷却塔方式を廃止する技術形成に鋭意傾注した。
この結果、冷却水配管系統を閉鎖配管とした地下水蓄熱槽を含む水流回路を採用し、媒体水を熱交換後に再度高度水処理手段により中水或いは飲料水として活用するシステムを完成し本発明に至った。
With the aim of eradicating Legionella spp., We focused our efforts on technology development to abolish the conventional cooling tower system, focusing on the effective intervention of groundwater as a medium that directly reflects the thermostatic properties of the underground.
As a result, a water flow circuit including a groundwater heat storage tank having a cooling water piping system as a closed pipe is adopted, and a system for utilizing medium water again as intermediate water or drinking water by advanced water treatment means after heat exchange is completed and the present invention is completed. It came.

即ち、本発明の要旨とするところは、恒久的な温度を維持する地下水を擁する地層帯まで掘削された深井戸(D)と、地下式コンクリート槽である蓄熱式水槽(B)と、地下水槽(A)と、吸収式冷温水発生器(C)とを含み、前記蓄熱式水槽(B)と前記地下水槽(A)とが、連通管(L13)を介して選択的に連通され、前記蓄熱式水槽(B)には、前記地下水が直接的に貯留され、前記蓄熱式水槽(B)に貯留された水を、前記吸収式冷温水発生器(C)の凝縮器冷却水として、または、前記蓄熱式水槽(B)に貯留された水の蓄熱エネルギーを、前記吸収式冷温水発生器(C)の熱交換器用熱源として、活用した後、前記地下水槽(A)および前記蓄熱式水槽(B)へと選択的に貯留するための配管(L11)を備え、前記地下水槽(A)および前記蓄熱式水槽(B)に貯留された水のうちの前者または双方を、用水として活用する手段を含むことを特徴とする給水システムにある。
ここで、前記用水として活用する手段として、前記地下水槽(A)に貯留された水を、濾過塔(イ)へと圧送するための原水ポンプ(P2)と、前記濾過塔(イ)にて前処理された濾過水を貯留するための中間処理水槽(T1)と、該中間処理水槽(T1)内の濾過水を、中水高架水槽(T4)へと貯留するための中水揚水ポンプ(P3)および中水揚水管(L4)と、前記中水高架水槽(T4)内のろ過水を、各中水利用施設へ供給するための中水供給管(L5)とを含むことを特徴とするものである。
また、前記用水として活用する手段として、前記地下水槽(A)に貯留された水を、濾過塔(イ)へと圧送するための原水ポンプ(P2)と、前記濾過塔(イ)にて前処理された濾過水を貯留するための中間処理水槽(T1)と、前記中間処理水槽(T1)へ貯留した濾過水を、膜濾過装置(ロ)へ圧送するための中間送水ポンプ(P4)と、前記膜濾過装置(ロ)で高度処理された処理水を、処理水槽(T2)に貯留するための処理水送水管(L12)と、前記処理水槽(T2)の処理水を、受水槽(T3)へ貯留するための処理水ポンプ(P5)および処理水管(L6)と、前記受水槽(T3)内の処理水を、上水高架水槽(T5)へ貯留するための上水揚水ポンプ(P7)および上水揚水管(L2)と、上水高架水槽(T5)内の処理水を、各水栓へ供給するための上水供給管(L3)とを含むものである。
上記、吸収式冷温水発生器(C)に係る冷却水の配管系統として、冷却水往管(L10)、冷却水還管(L11)を全て閉鎖配管システムとし大気等との接触を皆無とし、且つ、前記蓄熱式水槽(B)に貯留された水を一過式として前記冷却水往管(L10)の冷却水ポンプ(P6)にて、前記吸収式冷温水発生器(C)へと圧送させることにより、更に効率向上の追及可能なシステムとなる。
That is, the gist of the present invention is that a deep well (D) excavated to a geological zone having groundwater that maintains a permanent temperature, a regenerative water tank (B) that is an underground concrete tank, and a groundwater tank (A) and an absorption-type cold / hot water generator (C), and the thermal storage tank (B) and the underground water tank (A) are selectively communicated via a communication pipe (L13), In the regenerative water tank (B), the groundwater is directly stored, and the water stored in the regenerative water tank (B) is used as the condenser cooling water of the absorption cold / hot water generator (C), or After using the heat storage energy of the water stored in the heat storage water tank (B) as a heat source for the heat exchanger of the absorption cold / hot water generator (C), the ground water tank (A) and the heat storage water tank (B) provided with a pipe (L11) for selective storage into the groundwater tank The former or both of the water stored in A) and the thermal storage water tank (B), in the water supply system, characterized in that it comprises a means for utilizing the water.
Here, as means for utilizing as the irrigation water, a raw water pump (P2) for pumping water stored in the groundwater tank (A) to the filtration tower (A) and the filtration tower (I) An intermediate treated water tank (T1) for storing pretreated filtered water, and a middle water pumping pump (T4) for storing the filtered water in the intermediate treated water tank (T1) in an intermediate water elevated tank (T4) P3) and a middle water pumping pipe (L4), and a middle water supply pipe (L5) for supplying the filtered water in the middle water elevated water tank (T4) to each middle water use facility, To do.
Further, as means for utilizing the water, the raw water pump (P2) for pumping the water stored in the groundwater tank (A) to the filtration tower (A) and the filtration tower (A) An intermediate water tank (T1) for storing the treated filtered water, and an intermediate water pump (P4) for pumping the filtrate water stored in the intermediate water tank (T1) to the membrane filtration device (b) The treated water water pipe (L12) for storing treated water highly treated by the membrane filtration device (b) in the treated water tank (T2) and treated water in the treated water tank (T2) The treated water pump (P5) and the treated water pipe (L6) for storing in T3) and the treated water pump (P5) for storing the treated water in the water receiving tank (T3) in the elevated water tank (T5) P7) and the water pumping pipe (L2) and the treatment in the water elevated tank (T5) And it is intended to include a water supply pipe (L3) for supplying to each faucet.
As a cooling water piping system related to the absorption cold / hot water generator (C), the cooling water forward pipe (L10) and the cooling water return pipe (L11) are all closed piping systems and have no contact with the atmosphere, In addition, the water stored in the regenerative water tank (B) is temporarily transferred to the absorption cold / hot water generator (C) by the cooling water pump (P6) of the cooling water forward pipe (L10). By doing so, the system can be pursued for further improvement in efficiency.

ここで有効恒温性を活用可能な地下水とは、年間を通じ水温の変化の少ない地下水を対象とするもので、代表例で説明すると通常地下深度で100m程度の深井戸がその対象となる。この程度の地下水は、年中を通じ13ないし18℃の範囲内で推移しており、本発明の対象とする潜在熱エネルギーの活用媒体として好適である。
又、本発明で使用する蓄熱式地下水槽とは、断熱処置を施し接触による熱移動を阻止できる構造にて設営した水槽で、例えば隔壁として空間を挟む多重構造を取り入れる等にて達成できる。
Here, the groundwater that can utilize the effective isothermal property is intended for groundwater whose change in water temperature is small throughout the year, and a typical example is a deep well of about 100 m in the underground depth. This level of groundwater changes within a range of 13 to 18 ° C. throughout the year, and is suitable as a utilization medium of latent heat energy that is a subject of the present invention.
In addition, the heat storage type underground water tank used in the present invention is a water tank set up with a structure capable of preventing heat transfer by contact with heat insulation, and can be achieved, for example, by incorporating a multiple structure sandwiching a space as a partition wall.

吸収式冷温水発生器とは、二重効用吸収式冷凍機の事で、エネルギー源をガスとし、ガスの燃焼で生成された蒸気、高温水を使用し、冷媒は水で、吸収液に臭化リチウム水溶液を用いている。冷水と温水を同時又は別々に取り出すことが出来、高温再生器内の圧力が大気圧以下のため、関係法規の適用は受けない。又、他の冷凍機に比べて大型電動機が無く、振動・騒音が小さく、電力も少ないため環境にやさしいシステムである。
蓄熱式地下水槽で貯留された地下水の蓄熱エネルギーを、吸収式冷温水発生器の凝縮器・吸収器での冷却水、或いは冷却水熱交換器用熱源として活用させる事が出来る。
Absorption type cold / hot water generator is a double-effect absorption type refrigerator, which uses gas as energy source, steam and high-temperature water generated by gas combustion, refrigerant as water, and absorption liquid as odor. An aqueous lithium fluoride solution is used. Since cold water and hot water can be taken out simultaneously or separately and the pressure in the high-temperature regenerator is below atmospheric pressure, the relevant laws and regulations are not applied. Compared to other refrigerators, there is no large motor, vibration and noise are small, and power is low.
The heat storage energy of the groundwater stored in the regenerative groundwater tank can be used as cooling water in the condenser / absorber of the absorption cold / hot water generator or as a heat source for the cooling water heat exchanger.

地下水域内に潜在する熱エネルギーの活用方法は、揚水した地下水の有する全てのエンタルピーと、それ以外に無限に存在する変動水域内部の潜在的熱エネルギーの活用も対象可能となる。
例えば、環境条件の変動による自然エネルギーである気温の変位や地下深度による土中温度の変位等も活用可能となる。
The utilization method of the latent heat energy in the groundwater area can be applied to all the enthalpies of the pumped groundwater and the utilization of latent heat energy inside the infinitely variable water area.
For example, it is possible to utilize a change in temperature that is natural energy due to a change in environmental conditions, a change in soil temperature due to underground depth, and the like.

本発明は、従来着目されていない地下の無尽蔵な恒温性を、地下水を介しエンタルピーとして有効に活用する事により、省資源・レジオネラ属菌類撲滅対策を達成した有用な発明である。具体的には、地下水を効率的な水流回路を含む冷却方式の採用にある。
例えば、冷却水量において冷却水入り口温度を通常の冷却塔方式による32℃と地下水方式の20℃を対比すると、100USRTの能力ある吸収式冷凍機で冷却水量が通常の場合、冷却塔を使用し冷却水温度を32℃とするには、15L/min/ton〜13L/min/tonの水量が必要とする。しかし、地下水を直接利用するとして20℃の地下水を冷却水とすれば9L/min/ton〜7L/min/tonと想定出来ることになり、冷却水全体の水量を冷却塔方式に比べ80%〜70%の削減となる。
INDUSTRIAL APPLICABILITY The present invention is a useful invention that has achieved resource saving and legionella eradication measures by effectively utilizing infinite underground thermostat, which has not been focused on conventionally, as enthalpy through groundwater. Specifically, the groundwater is in a cooling system including an efficient water flow circuit.
For example, if the cooling water inlet temperature in the cooling water volume is 32 ° C by the normal cooling tower system and 20 ° C by the groundwater system, the cooling water volume is normal and the cooling water volume is normal by using an absorption refrigerator having a capacity of 100 USRT. In order to set the water temperature to 32 ° C., a water amount of 15 L / min / ton to 13 L / min / ton is required. However, if the groundwater at 20 ° C. is used as the cooling water when the groundwater is directly used, it can be assumed that it is 9 L / min / ton to 7 L / min / ton, and the total amount of cooling water is 80% compared to the cooling tower method. 70% reduction.

レジオネラ属菌類の撲滅対策による設備機能面での効果として、従来発生が懸念された冷却水系統の配管閉鎖要因の減少が大いに期待出来る。この事は、結果として冷却塔を不用と出来れば、更にこれら菌類自体の生息環境への影響として冷却水温が30℃付近である事から20℃付近にまで低下し、大気との接触を遮断出来るためにレジオネラ属菌類自体の生息を不能となし得るものである。
地球温暖化の原因となる二酸化炭素(CO2)等の温室効果ガスに対する抑制が叫ばれている状況の中、水道水1m3製造するのに発生する二酸化炭素(C02)の量を、環境庁の基準数量を0.6kg/m3と示されている。
一方すべからく、自己水源である地下水を利用し、高度処理する事による専用水道に変換した段階の二酸化炭素(CO2)の発生量を産出した結果について、以下の通り比較検討を実施し本発明の効果を具体的に示す。
As an effect on the equipment function by the countermeasure against the eradication of Legionella spp., It can be expected to greatly reduce the cause of the pipe closure of the cooling water system, which has been feared to occur. As a result, if the cooling tower can be dispensed with as a result, the temperature of the cooling water drops to around 20 ° C. as a result of the effects on the habitat of these fungi themselves, and the contact with the atmosphere can be cut off. Therefore, Legionella genus fungus itself can be disabled.
The amount of carbon dioxide (C02) generated to produce 1m3 of tap water in the situation where suppression of greenhouse gases such as carbon dioxide (CO2) causing global warming is called out The quantity is shown as 0.6 kg / m3.
On the other hand, the results of producing the amount of carbon dioxide (CO2) generated at the stage of conversion to a dedicated water supply using advanced groundwater using groundwater, which is a self-water source, were compared and examined as follows. Is specifically shown.

地下水利用による専用水道の建設、運用にかかる二酸化炭素(CO2)の排出量は、先ず建設、設置段階に於いて深井戸の掘削に使用する燃料、井戸用配管の素材、当システムのプラント設置設備の素材、資材、設備の輸送、据付に使用する燃料を試算した。
即ち、建設、設置段階の二酸化炭素排出量は、合計で塩化ビニール管使用の場合に0.004885kg/m3となった。次に、運用段階についての試算では電力使用に由来する二酸化炭素(CO2)の排出量は、0.305kg/m3との数値となった。概略区分数値を下記に明記する。
15m3/H処理プラント(2,628,000m3/30Y)=耐用年数を30年と設定した。
Carbon dioxide (CO2) emissions from the construction and operation of a dedicated water supply using groundwater are the fuel used for drilling deep wells, materials for well piping, and plant installation equipment for this system at the construction and installation stages. The fuel used for transportation and installation of materials, materials and equipment was estimated.
That is, the total carbon dioxide emissions at the construction and installation stages were 0.004885 kg / m3 when using vinyl chloride pipes. Next, in the trial calculation for the operation stage, the emission amount of carbon dioxide (CO2) derived from the use of electric power was a numerical value of 0.305 kg / m3. The general classification values are specified below.
15 m3 / H treatment plant (2,628,000 m3 / 30Y) = The service life was set to 30 years.

Figure 0004600680
Figure 0004600680

Figure 0004600680
Figure 0004600680

以上より、「表1」と「表2」に示す二酸化炭素(CO2)発生量の合計は、0.309885kg/m3となった。この数値は、水道水の値に対し、48.5%の削減率となった。
現状の飲料水供給システムでは、上水の基本生成過程から河川水の濾過、配水など工程が有る為にどうしても電気動力の消費によるCO2の排出が増大傾向にある。
しかし、本発明にて提案する如く上水と中水生成の一部に地下水を採用する事により、全量河川より生成される上水の使用される場合のCO2排出量と比較して、冷却水として自己水源の地下水を使用すればCO2排出量の約20%を削減出来る計算になる。
From the above, the total amount of carbon dioxide (CO2) generation shown in "Table 1" and "Table 2" was 0.309985 kg / m3. This figure was a 48.5% reduction rate relative to the value of tap water.
In the current drinking water supply system, since there are processes such as river water filtration and water distribution from the basic production process of clean water, the emission of CO2 due to the consumption of electric power inevitably tends to increase.
However, as proposed in the present invention, by adopting groundwater as part of the generation of clean water and intermediate water, the amount of cooling water compared to the amount of CO2 emitted when using the clean water generated from the river in its entirety is used. As a result, it is possible to reduce CO2 emissions by about 20% by using groundwater from its own water source.

更に、公共事業の一環として給水供給事業で延々とした配水管の延長上に各需要者が存在する現状で、一旦災害に遭遇した場合には配水管の寸断が惹起する懸念が大である。
このような不測の断水現象により、ライフラインとしての機能を失い、生命維持活動にも多大な影響を及ぼす状態は容易に首肯できる。
本発明による自己水源としての地下水の活用は、災害時の緊急ライフライン用給水としても極めて有効な手段となり得る。
以下実施例により、更に本発明を説明する。
Furthermore, in the present situation where each customer exists on the extension of the distribution pipe in the water supply business as part of public works, there is a great concern that the distribution pipe will be severed once a disaster is encountered.
Due to such an unexpected water-stopping phenomenon, it is possible to easily confirm a situation in which the function as a lifeline is lost and the life support activity is greatly affected.
The utilization of groundwater as a self-water source according to the present invention can be an extremely effective means for water supply for an emergency lifeline in the event of a disaster.
The following examples further illustrate the present invention.

本発明の実施の形態を図1に基づいて説明する。
図1に於ける深井戸(D)は、行政の規制範囲内で掘削されたもので、掘削深度は120m、不透水層を2層貫遂させ地表からの汚水とかの影響を受けない地下水である。
深度120m内外に於ける地層帯の地下水は、恒久的な温度を維持し年間を通じ18℃の平均水温を維持している。
又、行政の規制の範囲で揚水する事により、自然涵養とのバランスを維持し、環境との共生を推進する。尚、井水揚水ポンプ(P1)にて揚水した井水を井水揚水管(L1)を経て井水蓄熱槽(B)に貯留する。
An embodiment of the present invention will be described with reference to FIG.
The deep well (D) in Fig. 1 was excavated within the administrative limits of the government. The excavation depth is 120m, and it is groundwater that is not affected by sewage from the surface by passing through two impermeable layers. is there.
The groundwater in the geological zone at a depth of 120 m is maintained at a permanent temperature and an average water temperature of 18 ° C. throughout the year.
In addition, by pumping water within the scope of administrative regulations, we will maintain a balance with natural recharge and promote symbiosis with the environment. In addition, the well water pumped up by the well water pump (P1) is stored in the well water heat storage tank (B) through the well water pumping pipe (L1).

図1に於ける吸収式冷温水発生器(C)は、100USRTの能力を有し、冷水量1.0m3/min(冷水出口温度8℃の場合)設定で、冷却水量1.65m3/min(冷却水入り口温度31℃の場合)を必要とする。
ところが、井水を供給する事により冷却水入り口温度を20℃とすれば、上記の場合に冷却水量を40%減量する事が可能となる。
又、冷却水の配管系統として冷却水往(L10)、冷却水還管(L11)を全て閉鎖配管システムとし大気等との接触を皆無とし、且つ、井水蓄熱層(B)(「蓄熱式水槽」、「地下水蓄熱層」ともいう)に貯留された冷却水を一過式として冷却水往管(L10)の冷却水ポンプ(P6)にて、吸収式冷温水発生器(C)へと圧送させる事により更に効率向上の追及可能なシステムとなる。
The absorption-type cold / hot water generator (C) in FIG. 1 has a capacity of 100 USRT, and the cooling water amount is 1.65 m 3 / min (when the cold water outlet temperature is 8 ° C.). The cooling water inlet temperature is 31 ° C.).
However, if the cooling water inlet temperature is set to 20 ° C. by supplying well water, the amount of cooling water can be reduced by 40% in the above case.
The cooling water forward pipe as pipe system for cooling water (L10), the cooling water instead of pipe (L11) and all closed piping system and none contact with the atmosphere or the like, and, well water heat storage layer (B) ( "heat storage wherein the water tank "at" cooling water pump (P6 of cooling water往管 cooling water stored in the referred to also as ground water heat storage layer ") as a once-through (L10)), the absorption chiller generator to (C) It becomes a system that can pursue further efficiency improvement by pumping.

図1に於ける地下水蓄熱槽(B)は、地下式コンクリート槽でその内面に蓄熱槽用の断熱材を充填している。これにより地下水の有する熱エネルギーを保持させ、熱変化率を10%以内に抑え、地下水温度を20℃に保持出来る。地下水蓄熱槽(B)の容量は、800m3とし、必要冷却水量の10時間分を確保出来るものとした。
又、冷温水発生器の一日当たりの稼動時間は、冷却水量を30%削減可能となる点を考慮して1.15m3/minと設定し、8時間運転と想定して冷却水量を552m3/日とした。地下水揚水量は、500L/minにて随時補給出来る設定した。
地下水揚水ポンプ(P1)の稼動は、夏季の平常運転では、一日当たり13時間とすると500L/minの揚水ポンプで13時間稼動すると390m3/日となり、地下水蓄熱槽(B)の全容量800m3の約50%を確保出来得る。又、冬季に備え水槽間に設けた連通管(L13)を開放させて一体化すれば水質保持が確保出来ることになる。
The groundwater heat storage tank (B) in FIG. 1 is an underground concrete tank, and the inner surface is filled with a heat insulating material for the heat storage tank. Thereby, the thermal energy which groundwater has can be hold | maintained, a heat change rate can be suppressed within 10%, and groundwater temperature can be hold | maintained at 20 degreeC. The capacity of the groundwater heat storage tank (B) was 800 m3, and 10 hours of the required amount of cooling water could be secured.
The operating time per day of the cold / hot water generator is set to 1.15 m3 / min in consideration of the fact that the amount of cooling water can be reduced by 30%, and the amount of cooling water is set to 552 m3 / day on the assumption of 8-hour operation. It was. The groundwater pumping amount was set to be replenished at any time at 500 L / min.
The operation of the groundwater pump (P1) is 390m3 / day for 13 hours per day for normal operation in the summer, and 13 hours per day for 500L / min. 50% can be secured. In addition, if the communication pipe (L13) provided between the water tanks is opened and integrated in preparation for the winter, the water quality can be maintained.

図1に於ける地下水槽(A)は、上水、中水を製造する原水を貯留する水槽を示す。地下水槽(A)の容量は、300m3で、夏季の冷房時には吸収式冷温水発生器(C)の冷却水出口を地下水槽(A)に導入し、稼動済み冷却用水を原水として冷却水還管(L11)を経て貯留する。又、冬季には地下水蓄熱槽(B)に貯留した地下水は、連通管(L13)を経て地下水槽(A)に移行する。尚、原水を3種類に仕分けし、井戸原水、地下水蓄熱槽水、地下水槽水と各水槽の水質分析を定期的、季節毎に実施しながら水質管理を施す事が出来るものとした。
即ち、一旦冷却水として使用した地下水を地下水槽(A)にて貯留し、それを原水とし処理能力8m3/Hの濾過装置上水とし、一方同様に処理能力7m3/Hの濾過装置にて濾過して中水とし、夫々の使用目的に応じ合計15m3/Hの処理水を生成出来る装置とした。
The ground water tank (A) in FIG. 1 shows the water tank which stores the raw water which manufactures clean water and middle water. The capacity of the groundwater tank (A) is 300m3, and the cooling water outlet of the absorption-type cold / hot water generator (C) is introduced into the groundwater tank (A) during cooling in the summer, and the cooling water return pipe with the operating cooling water as raw water Store through (L11). In winter, the groundwater stored in the groundwater heat storage tank (B) is transferred to the groundwater tank (A) through the communication pipe (L13). In addition, the raw water was classified into three types, and it was assumed that water quality control could be performed while conducting water quality analysis of the well raw water, groundwater heat storage tank water, groundwater tank water and each tank regularly and every season.
That is, the groundwater once used as cooling water is stored in the groundwater tank (A), which is used as raw water to be filtered water with a processing capacity of 8 m3 / H, and similarly filtered through a filtering apparatus with a processing capacity of 7 m3 / H. In this case, the water was used as an apparatus capable of generating a total of 15 m 3 / H of treated water according to the purpose of use.

図1に於ける地下水槽(A)の上部に設置した地下水高度処理プラントでは、上水、中水を生成出来る。即ち、中水は直接中水用高架水槽(T4)へ中水揚水管(L4)を経て揚水し、以降は重力式にて中水供給管(L5)を経て各器具へ供給する。上水は、受水槽(T3)に導入し、市水(E)と混合出来る様に設定した。
井水の高度処理水は、水道法に則った飲料用水であり、上水高架水槽(T5)に上水揚水管(L2)を経て揚水、以下重力式にて上水供給管(L3)を経て各機器へ飲料水として供給出来る。
尚、受水槽(T3)には、給水本管より分岐した市水引込み管(ニ)を経て、上水のバックアップ用として100%の給水を確保した。
In the groundwater advanced treatment plant installed in the upper part of the underground water tank (A) in FIG. 1, it is possible to generate clean water and medium water. That is, the intermediate water is directly pumped to the intermediate water elevated tank (T4) through the intermediate water pumping pipe (L4), and thereafter supplied to each instrument by the gravity method through the intermediate water supply pipe (L5). The water was introduced into the water receiving tank (T3) and set so that it could be mixed with city water (E).
Well-treated water for well water is drinking water in accordance with the Water Supply Law. Pumped water is supplied to the elevated water tank (T5) via the water pumping pipe (L2), and the water supply pipe (L3) is connected by gravity. After that, it can be supplied to each device as drinking water.
In addition, the water receiving tank (T3) secured 100% water supply as a backup for clean water through a city water intake pipe (d) branched from the water supply main.

図1に示す設定を活用して、深度120mの深井戸を掘削し、これより地下水を揚水した。揚水試験の結果、地下水揚水量500L/minを確保出来た。原水の水質分析の結果、鉄1.23mg/L、マンガン0.066mg/L、色度7、濁度2.1で、水道法による飲料水の基準をクリアしていない事が判明した。尚、空調用としての水質では、硬度92mg/Lで基準値をクリアしていない事を確認した。
夏を想定して、外気温は36℃、地下水の水温を18℃と定め、本地下水を蓄熱式井水槽である地下水蓄熱槽(B)へ貯留したところ、地下水蓄熱槽での熱損失は0.8%で、19.6℃の水温を終日確保されており、地下水の恒温性を高効率で利用出来る事を確認した。
By utilizing the setting shown in FIG. 1, a deep well with a depth of 120 m was excavated, and groundwater was pumped from this. As a result of the pumping test, it was possible to secure a groundwater pumping amount of 500 L / min. As a result of water quality analysis of the raw water, it was found that iron 1.23 mg / L, manganese 0.066 mg / L, chromaticity 7 and turbidity 2.1, which did not satisfy the standards of drinking water by the Waterworks Law. It was confirmed that the water quality for air conditioning did not clear the standard value with a hardness of 92 mg / L.
Assuming summer, the outside air temperature is set to 36 ° C, the groundwater temperature is set to 18 ° C, and when this groundwater is stored in the groundwater storage tank (B), which is a regenerative well, the heat loss in the groundwater storage tank is zero. It was confirmed that the water temperature of 19.6 ° C was secured throughout the day at 8%, and that the constant temperature of the groundwater could be used with high efficiency.

揚水された地下水の熱エネルギー、即ち水温を保持する目的として断熱材機能を活用したコンクリート型枠工法を採用した。即ち、コンクリート型枠としてポリスチレンフォーム製のパネル(寸法1,000mm×250mm×10mmのブロック形状)、それをコンクリート打設後外さずに引き続き断熱材として活用し、表面は塗膜防水施工により蓄熱槽を構築した。塗膜防水材として、無溶剤型ウレタン樹脂の吹付施工を採用した。
その結果、蓄熱率95%の目標に対し、92%の保温蓄熱率を確保する事が出来た。
この工法を地上4階、地下1階で延面積2,580m2の病院建築に当システムを適用する為に、冷房負荷を計算上278,500Kcal/Hとして、吸収式冷温水発生器(C)の容量を100USRTと設定し。吸収式冷温水発生器の冷却水量は標準仕様で使用地下水温度が18℃の時に約8L/min/tonの基準を採用した。
従って、当機器の冷却水量を約800L/minとし、一過式を採用し冷却水ポンプ(P6)にて冷温水発生器(C)へ圧送した。
In order to maintain the thermal energy of the pumped-up groundwater, that is, the water temperature, a concrete formwork method utilizing a heat insulating material function was adopted. That is, a panel made of polystyrene foam (a block shape of dimensions 1,000 mm x 250 mm x 10 mm) as a concrete formwork, is used as a heat insulating material without removing it after placing the concrete, and the surface is a heat storage tank by coating film waterproofing Built. Spray coating of solventless urethane resin was adopted as a waterproof coating material.
As a result, it was possible to secure a heat storage rate of 92% against the target of 95%.
In order to apply this system to a hospital building with a floor area of 2,580m2 on the 4th floor above ground and 1st floor below, the cooling load is calculated as 278,500Kcal / H and the absorption cold / hot water generator (C) Set the capacity to 100 USRT. The amount of cooling water in the absorption cold / hot water generator was standard, and a standard of about 8 L / min / ton was adopted when the groundwater temperature used was 18 ° C.
Therefore, the amount of cooling water of this device was set to about 800 L / min, a one-time system was adopted, and pumped to the cold / hot water generator (C) by the cooling water pump (P6).

本実験で、100USRTの吸収式冷温水発生器(C)に対し、低水温(19.6℃)の冷却水を一過式にて供給し、冷却水量は8.7L/min/tonと確認出来た。
即ち、870L/minとなり、稼動時間を8時間とすると417.6m3/Dとなった。この数値は、冷却塔方式に比べて、33.8%の削減となった。井水蓄熱槽(B)の容量は、800m3に対し約15時間分を貯留出来る結果をも確認出来省資源・省エネに対応させる事が出来た。
尚、井水蓄熱槽(B)の容量の50%を補給するものとすれば、井水揚水量は24時間稼動で280L/minで供給する事となりシステム稼動が可能である事を確認出来、揚水量の削減となった。
しかし、蓄熱効率の維持及び容量の安全率を鑑み、全容量の30%の削減に留める事とし、井水蓄熱槽(B)の常時貯留量を560m3とした。尚、井水揚水量は、20時間稼動とし、450L/minとなった。
In this experiment, low-temperature (19.6 ° C.) cooling water was supplied to the 100 USRT absorption-type cold / hot water generator (C) in a transient manner, and the amount of cooling water was confirmed to be 8.7 L / min / ton. done.
That is, it was 870 L / min, and when the operation time was 8 hours, it was 417.6 m 3 / D. This figure was 33.8% reduction compared to the cooling tower method. The capacity of the well water storage tank (B) was able to confirm the result of storing about 15 hours for 800m3, and was able to cope with resource saving and energy saving.
If 50% of the capacity of the well water storage tank (B) is to be replenished, the well water pumping capacity will be supplied at 280 L / min for 24 hours operation, confirming that the system can be operated. The amount of pumped water was reduced.
However, considering the maintenance of heat storage efficiency and the safety factor of capacity, it was decided to reduce it to 30% of the total capacity, and the constant storage amount of the well water heat storage tank (B) was set to 560 m 3. The well water yield was 450 L / min after 20 hours of operation.

地下水を使用する場合の難点として、空調機に与える影響が多大となる事が考えられ、水道水々質に比して硬度が高い点でスケールが沈着する懸念があった。この懸念を考慮し、空調用の補給水の硬度基準70mg/L以下に保持するために、空調機、配管等の除錆、防錆の効果確認を行った結果を以下に示す。
図1より、中水揚水管(L4)、処理水管(L6)、冷却水往管(L10)の各配管に磁力線照射器(ハ)を設置し、電磁力によるスケール防止効果を確認する事にした。その結果は、次の表3に示すとおりとなった。
When groundwater is used, it is considered that the influence on the air conditioner becomes great, and there is a concern that the scale is deposited in that the hardness is higher than the quality of tap water. In consideration of this concern, the results of confirming the effect of rust removal and rust prevention of air conditioners, pipes, etc. in order to keep the hardness standard of supplementary water for air conditioning at 70 mg / L or less are shown below.
From Fig. 1, a magnetic field irradiator (c) is installed in each pipe of the intermediate water pumping pipe (L4), treated water pipe (L6), and cooling water outgoing pipe (L10) to confirm the scale prevention effect by electromagnetic force. did. The results are shown in Table 3 below.

Figure 0004600680
Figure 0004600680

表3の結果により、磁力線照射により硬度が空調用に使用可能とする規定以下の水質に果然する事が出来た。又、除錆防錆に対し多大な影響を及ぼす鉄分に対し、中水揚水管系統、処理水管系統共に濾過塔(イ)を通過している為、更に鉄分の処理効率が上がり水道法に則る飲料水に適合する水質になり得た。
そこで、X線解析を実施した結果、当初FeOの状態が6ヶ月後にはFe3O4(マグネタイト)に変化している事が確認出来た。
従って、配管、熱交換器等の除錆、防錆の効果が顕著に発揮されており、環境面から考察するに薬注、水処理、清掃、維持管理、予防保繕等の観点からして煩雑な特別管理維持を不要とするシステムを確立出来たものと評価した。
すべからく、当初のレジオネラ属菌については冷却水温度の低下にて当然発生が抑制されている状態を現出しているが、更に電磁による菌の抑制効果が発揮出来うる事を確認した。
From the results shown in Table 3, the water quality was reduced to a level below the standard that allows the use of air-conditioning for air conditioning. In addition, the iron content that greatly affects rust removal and rust prevention passes through the filtration tower (b) for both the middle water pumping pipe system and the treated water pipe system. The water quality could be suitable for drinking water.
Therefore, as a result of X-ray analysis, it was confirmed that the state of FeO initially changed to Fe3O4 (magnetite) after 6 months.
Therefore, the effects of rust removal and rust prevention of pipes, heat exchangers, etc. are exerted remarkably, and from the viewpoint of chemical injection, water treatment, cleaning, maintenance, preventive maintenance, etc., from the environmental viewpoint. It was evaluated that a system that did not require complicated special management maintenance could be established.
In all, the original Legionella genus has been shown to be naturally suppressed by a decrease in the cooling water temperature, but it has been confirmed that the effect of inhibiting the bacteria by electromagnetics can be exerted.

図1の設定で、地下水蓄熱槽(B)に貯留されていた恒温の地下水を、吸収式冷温水発生器(C)の冷却水として活用後、廃棄せずに地下水槽(A)に再度貯留し各種用水の原水とした。
水質に関し原水の水質面に変化は無いとして、冬季を想定し市水は5℃程度に低下するので、原水温度を17.8℃に調整した。この温度にしても、その差異は大幅に維持されており、井水槽の熱損失を0.6℃程度に見積もれば良い。以下、この条件下で実験を続行した。
尚、井水蓄熱槽(B)と井水槽(A)との隔壁に連通管(L13)を設け、一定した水位と水温を保持するための装置を布置し、井水揚水ポンプ(P1)の作動を自動的に制御した。
又、地下水槽(A)の容量を300m3と設定し必要給水量を上水用として8m3/H、中水用として7m3/H、合計15m3/Hの1日分を確定出来た。この結果、安定した原水を確保する事が可能となった。
The constant temperature groundwater stored in the groundwater heat storage tank (B) with the setting shown in Fig. 1 is used as cooling water for the absorption cold / hot water generator (C), and then stored again in the groundwater tank (A) without being discarded. It was used as raw water for various types of water.
Assuming that there is no change in the quality of raw water in terms of water quality, city water drops to about 5 ° C in the winter, so the raw water temperature was adjusted to 17.8 ° C. Even at this temperature, the difference is largely maintained, and the heat loss of the well tank may be estimated to about 0.6 ° C. Hereinafter, the experiment was continued under these conditions.
In addition, a communication pipe (L13) is provided in the partition wall between the well-water heat storage tank (B) and the well-water tank (A), a device for maintaining a constant water level and water temperature is laid, and the well-water pump (P1) Operation was controlled automatically.
Moreover, the capacity of the groundwater tank (A) was set to 300 m3, and the required water supply amount was 8 m3 / H for clean water, 7 m3 / H for middle water, and a total of 15 m3 / H for one day could be determined. As a result, it became possible to secure stable raw water.

図1に基づき地下水槽(A)に貯留している300m3の原水を、原水ポンプ(P2)(50×40)×15m3/H×25mH×2.2kwにて濾過塔(イ)へ圧送した。圧送された原水は濾過塔にて地下水中に一般的に含まれている鉄、マンガン等のいわゆる金気を除去した。
又、濾過塔は原水中に鉄、マンガンが基準値以下で色度、濁度共に飲料適性である場合でも、後段の膜濾過の負荷を軽減させるための前処理の役割を担った。
尚、濾過塔の効率を良くし能力を発揮させる為並びに殺菌の役割を兼ね備える次亜塩素酸ソーダを原水供給管(L7)に注入した。次亜塩素酸ソーダ槽を300Lとし、薬注ポンプの能力を16ml/min×0.98MPa×16Wを2台採用した。注入量は、上水系統末端水栓にて、水道法に決められている残留塩素(遊離)0.1mg/Lを確保出来得る様に設定した。
300 m3 of raw water stored in the groundwater tank (A) based on FIG. 1 was pumped to the filtration tower (I) with a raw water pump (P2) (50 × 40) × 15 m3 / H × 25 mH × 2.2 kW. The pumped raw water removed so-called gold, such as iron and manganese, generally contained in the groundwater by a filtration tower.
Further, the filtration tower played a role of pretreatment for reducing the membrane filtration load in the subsequent stage even when iron and manganese in the raw water were below the standard values and both chromaticity and turbidity were suitable for beverages.
In addition, in order to improve the efficiency of the filtration tower and to exhibit its ability, sodium hypochlorite having a role of sterilization was injected into the raw water supply pipe (L7). The sodium hypochlorite tank was set to 300 L, and the capacity of the chemical injection pump was 2 units of 16 ml / min × 0.98 MPa × 16 W. The injection amount was set so that 0.1 mg / L of residual chlorine (free) determined by the Waterworks Law could be secured at the water tap end tap.

図1より、濾過塔(イ)にて前処理された濾過水を、中間処理水槽(T1)に貯留した。以後、中間処理水槽内の濾過水を中水用としての水質が対応可能につき、中水揚水ポンプ(P3)により中水揚水管(L4)を経て、中水高架水槽へ貯留した。それ以降の通水は重力式にて中水供給管(L5)を経て各中水利用施設へ供給した。尚、中間処理水槽(T1)は、10m3とした。
前処理された濾過水を中間処理水槽(T1)へ貯留し、以後中間送水ポンプ(P4)にて、後段の高度処理である膜濾過装置(ロ)へ圧送した。膜濾過装置で高度処理された処理水を、処理水送水管(L12)を経て、処理水槽(T2)に貯留した。処理水槽(T2)の容量を6m3とし、水道法に則った上水と同等の水質に精製した。
以降、処理水ポンプ(P5)にて、処理水管(L6)を経て受水槽(T3)へ貯留した。受水槽(T3)容量は80m3とし、上水揚水ポンプ(P7)にて上水揚水管(L2)を経て、上水高架水槽(T5)へ貯留し、以後重力式にて上水供給管より各水栓へ供給した。
尚、給水供給のバックアップ機能として又、上水を100%の供給量に対応すべく上水管(E)を設け、上水引き込み管(ニ)を経て供給可能にした。
From FIG. 1, the filtered water pretreated in the filtration tower (A) was stored in the intermediate treated water tank (T1). Thereafter, the filtered water in the intermediate treated water tank can be used for the quality of the medium water, and it was stored in the medium water elevated tank through the medium water pumping pipe (L4) by the medium water pump ( P3 ). After that, the water was supplied to each facility for use of intermediate water through the intermediate water supply pipe (L5) by gravity. The intermediate treatment water tank (T1) was 10 m3.
The pretreated filtered water was stored in the intermediate treatment water tank (T1), and then was pumped to the membrane filtration apparatus (b), which is a subsequent advanced treatment, by the intermediate water pump (P4). The treated water that was highly treated by the membrane filtration device was stored in the treated water tank (T2) via the treated water feed pipe (L12). The capacity of the treated water tank (T2) was 6 m3, and it was refined to a water quality equivalent to tap water in accordance with the Waterworks Law.
Thereafter, it was stored in the water receiving tank (T3) through the treated water pipe (L6) by the treated water pump ( P5 ). Receiving tank (T3) capacity is 80m3, stored in the elevated water tank (T5) via the upper water pumping pipe (L2) by the upper water pump (P7), and then from the upper water supply pipe by gravity. Supplied to each faucet.
In addition, as a backup function of the water supply, a water pipe (E) is provided so as to correspond to a supply amount of 100% of the water, and the water can be supplied via the water intake pipe (d).

地下水の恒温性蓄熱エネルギーを、給湯器の熱源削減に大きく貢献させる事が出来る。
即ち、冬季においての市水温度は平均5℃であり、給湯器の供給水とすればエネルギー効率を極めて低下せしめる事が考えられる。
しかし、本発明の方式では地下水槽水の水温を平均17.2℃程度に保持できると想定できるので極めて有利となる。即ち、当病院の総給湯量を45,000L/日として供給水のエネルギーを消費するものとして比較した結果、下記の如く考察出来る。
条件として給湯温度:60℃、総給湯量:45,000L/日、上水温度:5℃、地下水槽温度17.2℃とすると次の通りとなる。
上水の場合:
加熱能力=45,000X1/10(60−5)=247,500kcal/H・・・A
地下水槽水の場合:
加熱能力=45,000X1/10(60−17.2)=192,600kcal/H・・・B
削減率=B÷A=0.75X100=75%
以上の結果、地下水の潜在エンタルピーの有効活用による25%の削減省資源・省エネを確認する事が出来た。
The constant temperature storage energy of groundwater can greatly contribute to the reduction of the heat source of water heaters.
That is, the city water temperature in winter is an average of 5 ° C., and it can be considered that the energy efficiency is extremely reduced if the water is supplied to the water heater.
However, the method of the present invention is extremely advantageous because it can be assumed that the water temperature of the underground water tank can be maintained at an average of about 17.2 ° C. That is, as a result of comparing the hospital with the total hot water supply amount of 45,000 L / day and consuming the energy of the supplied water, it can be considered as follows.
As conditions, hot water supply temperature: 60 ° C., total hot water supply amount: 45,000 L / day, clean water temperature: 5 ° C., groundwater tank temperature: 17.2 ° C.
For clean water:
Heating capacity = 45,000 × 1/10 (60−5) = 247,500 kcal / H... A
For underground aquarium water:
Heating capacity = 45,000 × 1/10 (60−17.2) = 192,600 kcal / H... B
Reduction rate = B ÷ A = 0.75X100 = 75%
As a result of the above, we were able to confirm a 25% reduction in resource and energy savings by effectively utilizing the potential enthalpy of groundwater.

全ゆる災害の中で、飲料水系ライフラインのダメージが最大なのが地震災害と云われる。最近の地震災害における水道本管の破損は著しく、断水と復旧の困難さを露呈し被災民の生命維持、保健衛生維持に最大の支障を来たしている。
この断水状況による影響は、医療施設を初めとして人命を失う元凶となった。特に人命を救う役割を担っている病院においては、致命的な結果を生んでいる。
この様な状況下、本発明による如く市水以外に地下水による自己水源を保持する事により、電源の確保さえ可能ならば生命維持並びに業務継続が確保出来得る事が明白である。
更に最近発生した地震の教訓におおいても、井戸設備が破損したとの報告は皆無で生命維持の給水を供給出来たとの事実に接し、地下水確保の重要性を意識せざるを得ない。
Of all the disasters, the greatest damage to the drinking water lifeline is said to be an earthquake disaster. Damage to the water main in recent earthquake disasters has been remarkable, and it has been the biggest obstacle to maintaining the life and health of affected people due to the difficulty of water cut and restoration.
The impact of this water outage became the main cause of losing human lives, starting with medical facilities. Especially in hospitals that are responsible for saving lives, fatal consequences have been produced.
Under such circumstances, it is obvious that by maintaining a self-water source using groundwater in addition to city water as in the present invention, life maintenance and business continuity can be secured if it is possible to secure a power source.
Furthermore, in the lessons learned from recent earthquakes, it was necessary to be aware of the importance of securing groundwater in the face of the fact that there was no report that well facilities were damaged and that water for life support could be supplied.

以上に詳説したように、本発明は地下に保有されるエンタルピーを地下水の媒体を介してその一部を有効に活用し、更に地下水を無駄にすることなく高度処理機能のシステムに組み込み、引いては省資源性、炭酸ガス抑制等の環境改善に有用なシステム構築を可能にしたものである。
又、地下水の水質に何らの影響を及ぼさず、人体に対する健康の面に対しても問題を起こさない自然のエネルギーの活用こそ、真の人類生活に貢献できるものと確信する。
本発明による第1の特徴は、地下の恒温性を活用するに地下水を媒体とした点にあり、地下の無尽蔵たるエンタルピーの一部を利用する一過式のシステムとした点にある。
本発明による第2の特徴は、低水温を保持した地下水を冷温水発生器の冷却媒体として活用し、一過式のシステムにて冷却水量を削減を達成するシステムとしている点にある。
これらシステムの導入により、人工熱の発生を抑止する技術発展の先駆的分野を発展させることに繋がり、今後の産業発展を牽引する工業的効果は多大で有るものと確信する。
As described in detail above, the present invention effectively utilizes a portion of the enthalpy retained underground through a medium of groundwater, and further incorporates and subtracts it into a system for advanced processing functions without wasting groundwater. Enables the construction of a system useful for improving the environment, such as resource saving and carbon dioxide suppression.
I am convinced that the use of natural energy that does not affect the quality of groundwater and does not cause any problems in the health of the human body can contribute to real human life.
The first feature of the present invention is that groundwater is used as a medium for utilizing the thermostatic property of the underground, and that it is a transient system that uses a part of the infinite underground enthalpy.
The second feature of the present invention resides in that groundwater having a low water temperature is utilized as a cooling medium for a cold / hot water generator, and a system that achieves a reduction in the amount of cooling water in a transient system.
The introduction of these systems will lead to the development of a pioneering field of technological development that suppresses the generation of artificial heat, and we are convinced that the industrial effects that will drive future industrial development are enormous.

本発明の実施例で、本発明のフローシートを示すものである。  The Example of this invention shows the flow sheet of this invention.

符号の説明Explanation of symbols

A 地下水槽
B 地下水蓄熱槽
C 吸収式冷温水発生器
D 井戸
E 市水
T1 中間処理水槽
T2 処理水槽
T3 受水槽
T4 中水高架水槽
T5 上水高架水槽
イ 濾過塔
ロ 膜濾過装置
ハ 磁力線照射器
ニ 市水引き込み管
P1 地下水揚水ポンプ
P2 原水ポンプ
P3 中水揚水ポンプ
P4 中間送水ポンプ
P5 処理水ポンプ
P6 冷却水ポンプ
P7 上水揚水ポンプ
L1 井水揚水管
L2 上水揚水管
L3 上水供給管
L4 中水揚水管
L5 中水供給管
L6 処理水管
L7 原水供給管
L8 冷温水往管
L9 冷温水還管
L10 冷却水往管
L11 冷却水還管
L12 処理水送水管
L13 連通管
A Groundwater tank B Groundwater heat storage tank C Absorption type cold / hot water generator D Well E City water T1 Intermediate treatment water tank T2 Treatment water tank T3 Receiving tank T4 Medium water elevated water tank T5 Water elevated water tank B Filtration tower B Membrane filtration device C Magnetic field irradiation device D Water supply pipe P1 Groundwater pump P2 Raw water pump P3 Middle water pump P4 Intermediate water pump P5 Treatment water pump P6 Cooling water pump P7 Water pumping pump L1 Well water pumping pipe L2 Water pumping pipe L3 Water supply pipe L4 Middle water pumping pipe L5 Middle water supply pipe L6 Raw water supply pipe L7 Raw water supply pipe L8 Cold / hot water outgoing pipe L9 Cold / hot water return pipe L10 Cooling water outgoing pipe L11 Cooling water return pipe L12 Treated water supply pipe L13 Communication pipe

Claims (4)

恒久的な温度を維持する地下水を擁する地層帯まで掘削された深井戸(D)と、地下式コンクリート槽である蓄熱式水槽(B)と、地下水槽(A)と、吸収式冷温水発生器(C)とを含み、
前記蓄熱式水槽(B)と前記地下水槽(A)とが、連通管(L13)を介して選択的に連通され、
前記蓄熱式水槽(B)には、前記地下水が直接的に貯留され、
前記蓄熱式水槽(B)に貯留された水を、前記吸収式冷温水発生器(C)の凝縮器冷却水として、または、前記蓄熱式水槽(B)に貯留された水の蓄熱エネルギーを、前記吸収式冷温水発生器(C)の熱交換器用熱源として、活用した後、前記地下水槽(A)および前記蓄熱式水槽(B)へと選択的に貯留するための配管(L11)を備え、前記地下水槽(A)および前記蓄熱式水槽(B)に貯留された水のうちの前者または双方を、用水として活用する手段を含むことを特徴とする給水システム。
Deep wells (D) excavated to the geological zone holding groundwater to maintain a permanent temperature, thermal storage tanks (B) that are underground concrete tanks, groundwater tanks (A), and absorption cold / hot water generators (C) and
The regenerative water tank (B) and the underground water tank (A) are selectively communicated via a communication pipe (L13),
The groundwater is directly stored in the thermal storage tank (B),
The water stored in the regenerative water tank (B) is used as the condenser cooling water of the absorption cold / hot water generator (C), or the heat storage energy of water stored in the regenerative water tank (B), As a heat source for the heat exchanger of the absorption-type cold / hot water generator (C), a pipe (L11) for selectively storing in the ground water tank (A) and the heat storage water tank (B) is provided. The water supply system characterized by including means for utilizing the former or both of the water stored in the underground water tank (A) and the regenerative water tank (B) as irrigation water.
前記用水として活用する手段として、前記地下水槽(A)に貯留された水を、濾過塔(イ)へと圧送する原水ポンプ(P2)と、前記濾過塔(イ)にて前処理された濾過水を貯留するための中間処理水槽(T1)と、該中間処理水槽(T1)内の濾過水を、中水高架水槽(T4)へと貯留するための中水揚水ポンプ(P3)および中水揚水管(L4)と、前記中水高架水槽(T4)内のろ過水を、各中水利用施設へ供給するための中水供給管(L5)とを含むことを特徴とする請求項1記載の給水システム。As means for utilizing as the irrigation water, the raw water pump (P2) for pumping the water stored in the groundwater tank (A) to the filtration tower (A) and the filtration pretreated by the filtration tower (A) An intermediate treated water tank (T1) for storing water, and a middle water pump (P3) and intermediate water for storing filtered water in the intermediate treated water tank (T1) into an intermediate water elevated tank (T4) The water supply pipe (L4) and the middle water supply pipe (L5) for supplying the filtrate in the said middle water elevated water tank (T4) to each middle water utilization facility are characterized by the above-mentioned. Water supply system. 前記用水として活用する手段として、前記地下水槽(A)に貯留された水を、濾過塔(イ)へと圧送するための原水ポンプ(P2)と、前記濾過塔(イ)にて前処理された濾過水を貯留するための中間処理水槽(T1)と、前記中間処理水槽(T1)へ貯留した濾過水を、膜濾過装置(ロ)へ圧送するための中間送水ポンプ(P4)と、前記膜濾過装置(ロ)で高度処理された処理水を、処理水槽(T2)に貯留するための処理水送水管(L12)と、前記処理水槽(T2)の処理水を、受水槽(T3)へ貯留するための処理水ポンプ(P5)および処理水管(L6)と、前記受水槽(T3)内の処理水を、上水高架水槽(T5)へ貯留するための上水揚水ポンプ(P7)および上水揚水管(L2)と、上水高架水槽(T5)内の処理水を、各水栓へ供給するための上水供給管(L3)とを含むことを特徴とする請求項1または2記載の給水システム。As means for utilizing the water, the water stored in the groundwater tank (A) is pretreated by the raw water pump (P2) for pumping the water to the filtration tower (A) and the filtration tower (A). An intermediate water tank (T1) for storing filtered water, an intermediate water pump (P4) for pumping filtrate water stored in the intermediate water tank (T1) to a membrane filtration device (b), A treated water supply pipe (L12) for storing treated water highly treated by the membrane filtration device (b) in the treated water tank (T2), and treated water in the treated water tank (T2) are received in the water receiving tank (T3). Treated water pump (P5) and treated water pipe (L6) for storing water and treated water in the water receiving tank (T3) in a water supply elevated water tank (T5) And treated water in the water pumping pipe (L2) and the elevated water tank (T5), Claim 1 or 2 water supply system according to comprising water supply pipe for supplying the faucet and (L3). 前記吸収式冷温水発生器(C)に係る冷却水の配管系統として、冷却水往管(L10)、冷却水還管(L11)を全て閉鎖配管システムとし大気等との接触を皆無とし、且つ、前記蓄熱式水槽(B)に貯留された水を一過式として前記冷却水往管(L10)の冷却水ポンプ(P6)にて、前記吸収式冷温水発生器(C)へと圧送させることを特徴とする請求項1から3のいずれか1項記載の給水システム。As the cooling water piping system for the absorption-type cold / hot water generator (C), the cooling water forward pipe (L10) and the cooling water return pipe (L11) are all closed piping systems, and there is no contact with the atmosphere, and The water stored in the regenerative water tank (B) is made into a transient type and pumped to the absorption cold / hot water generator (C) by the cooling water pump (P6) of the cooling water forward pipe (L10). The water supply system of any one of Claims 1-3 characterized by the above-mentioned.
JP2006037198A 2006-01-18 2006-01-18 Water supply system Expired - Lifetime JP4600680B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2006037198A JP4600680B2 (en) 2006-01-18 2006-01-18 Water supply system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2006037198A JP4600680B2 (en) 2006-01-18 2006-01-18 Water supply system

Publications (2)

Publication Number Publication Date
JP2007192004A JP2007192004A (en) 2007-08-02
JP4600680B2 true JP4600680B2 (en) 2010-12-15

Family

ID=38447915

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006037198A Expired - Lifetime JP4600680B2 (en) 2006-01-18 2006-01-18 Water supply system

Country Status (1)

Country Link
JP (1) JP4600680B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103774723A (en) * 2012-10-26 2014-05-07 上海管道纯净水股份有限公司 Manual well device for air-energy heat pump

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101256876B1 (en) * 2011-03-03 2013-04-22 삼중테크 주식회사 Hybrid absorption type air conditioning system
CN102505731A (en) * 2011-10-24 2012-06-20 武汉大学 Groundwater acquisition system under capillary-injection synergic action
JP5963570B2 (en) * 2012-06-28 2016-08-03 株式会社ウェルシィ Groundwater purification apparatus and operation method thereof
JP5963790B2 (en) * 2014-02-14 2016-08-03 株式会社守谷商会 Groundwater circulation type geothermal heat collection system and geothermal use air conditioning or hot water supply system

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5696261U (en) * 1979-12-24 1981-07-30
JPH07185573A (en) * 1993-12-28 1995-07-25 Hitachi Ltd Water treatment system and water treatment method
JP2005313137A (en) * 2004-04-29 2005-11-10 Uerushii:Kk Regular and emergency drinking water supply system
JP2006046677A (en) * 2004-07-30 2006-02-16 Techno Trade:Kk Utilization system of ground water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103774723A (en) * 2012-10-26 2014-05-07 上海管道纯净水股份有限公司 Manual well device for air-energy heat pump

Also Published As

Publication number Publication date
JP2007192004A (en) 2007-08-02

Similar Documents

Publication Publication Date Title
US6393775B1 (en) Utilities container
CN103608522B (en) Method and system for sustainable cooling of industrial processes
US7481924B2 (en) Cooling medium flow passage
CA2901700C (en) Systems and methods for recovering energy from wastewater
US20140250931A1 (en) Seasonal thermal energy storage system
US20020189173A1 (en) Utilities container
KR101283349B1 (en) Tube well type heat pump system for removing and sterilizing foreign material and air
Davis et al. Case study: Los Angeles water services restoration following the 1994 Northridge earthquake
WO2005103595A1 (en) Disinfection system
Hepbasli Current status of geothermal energy applications in Turkey
JP4600680B2 (en) Water supply system
Khujaev et al. RETRACTED: Modernization of existing infrastructure, heat supply systems
Lund Direct Utilization of Geothermal Resources Worldwide
US20140202565A1 (en) Modular community water station
JP6755084B2 (en) Legionella spp. Countermeasure system, cooled body cooling system, Legionella spp. Countermeasure method and cooled body cooling method of water-cooled substation
KR20110036241A (en) Local air-conditioning and hot water supply using seawater and operation method according to efficient configuration of the system
JP2005313137A (en) Regular and emergency drinking water supply system
JP2005029963A (en) Lifeline tower
JP2008155190A (en) Quality active drinking water supply system and apparatus
KR101166332B1 (en) Applicable heat-exchanging circulation water terminal pool system for large quantity requirement of seawater heat and/or geothermal heating and warm water supply, and it's effective operation method
KR102327523B1 (en) Green Energy system with suppling water and geothermal heat
KR102043892B1 (en) Heating water supply structure of district heating system
Blaga et al. Possible Geothermal District Heating in Sanmartin, Romania
Ranjan et al. Operating experience of desalination unit coupled to primary coolant system of CIRUS
Micallef Potential energy savings when using saline water for cooling chillers in Malta

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20090115

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20100624

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100706

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100823

RD03 Notification of appointment of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7423

Effective date: 20100823

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20100908

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20100914

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131008

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 4600680

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250