JP2009291729A - Spa-water gas separator - Google Patents

Spa-water gas separator Download PDF

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JP2009291729A
JP2009291729A JP2008148886A JP2008148886A JP2009291729A JP 2009291729 A JP2009291729 A JP 2009291729A JP 2008148886 A JP2008148886 A JP 2008148886A JP 2008148886 A JP2008148886 A JP 2008148886A JP 2009291729 A JP2009291729 A JP 2009291729A
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gas
water
hot spring
spa
outside air
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Yoshiyuki Tokumaru
義幸 徳丸
Kazuya Momo
和弥 百々
Hidehito Suzaki
秀人 須崎
Manabu Mizawa
学 見澤
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EONEX KK
Maywa Co Ltd
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EONEX KK
Maywa Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a spa-water gas separator for safely separating, diffusing, and diluting gas to be separated by practicing combined water-spray, ventilation, and moisture-reduction and for preventing secondary damage such as spa-scale generation, a spa-water temperature fall, and white-smoke generation. <P>SOLUTION: In area 1, the spa water is sprayed onto an impact plate to separate the gas from the spa water and diffuse the gas. Then, the separated gas is diluted with primary outside air blow to prevent the hazard due to gas toxicity or explosion and, on the other hand, to reduce the partial pressure of the gas component to be separated in the system to enhance the separation performance of the system. In area 2, moisture is removed to prevent the white-smoke generation at an exhaust outlet and secondary outside air is blown in to approximate the temperature of the exhaust gas to that of the outside air and, at the same time, to dilute the concentration of the gas to that corresponding to the safety factor according to the kind of the gas component. In area 3, a silencer is installed to prevent the noise of the exhaust gas. Area 6, a spa-water storage, is ventilated via an exhaust pipe 114 to prevent the gas retention in the area. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、温泉水を揚湯するに当り付随して発生するガスを安全に分離、拡散及び希釈する装置にかかり効率的且つ効果的なガス分離、拡散及び希釈を行う一方、副作用として発生する温泉スケール発生、温泉水の温度降下及び白煙の発生という問題の防止又は抑制を実現するガス分離装置に関するものである。   The present invention relates to an apparatus for safely separating, diffusing and diluting gas generated accompanying hot water from hot spring water, and performs efficient and effective gas separation, diffusion and dilution, while occurring as a side effect. The present invention relates to a gas separation device that realizes prevention or suppression of problems of hot spring scale generation, temperature drop of hot spring water, and generation of white smoke.

従来、温泉水の利用に当りポンプで揚湯し水槽に貯留しヘンリーの法則により大気へ温泉水中のガスが自然放出される現象を利用してきた。然しこの方法では当該温泉水に対する分離対象ガスの飽和溶解濃度以下とすることが難しく、分離対象ガスが温泉水中に残留又は溶存し風呂などの利用施設内で温泉水から分離対象ガスが放出され成分により爆発、燃焼、酸欠又は有害ガスによる健康被害の問題があった。   In the past, hot spring water has been pumped up and stored in a water tank, and the phenomenon in which hot spring water gas is spontaneously released to the atmosphere by Henry's law has been used. However, in this method, it is difficult to make the concentration of the separation target gas below the saturation dissolution concentration in the hot spring water, the separation target gas remains or dissolves in the hot spring water, and the separation target gas is released from the hot spring water in a facility such as a bath. There was a problem of health damage due to explosion, combustion, lack of oxygen or harmful gas.

又、従来の技術では分離対象ガスの特性によって爆発の危険性があるため水槽に煙突を設置し煙突上部に特殊金網を取り付け水槽内への火気の侵入防止を図ってきた。然しこの方法では水槽内に高濃度のガスが滞留し爆発する危険性に対して不十分という問題があった。   In the prior art, because there is a risk of explosion due to the characteristics of the gas to be separated, a chimney is installed in the aquarium, and a special wire net is attached to the top of the chimney to prevent the intrusion of fire into the aquarium. However, this method has a problem that it is insufficient for the danger of high concentration gas staying in the water tank and exploding.

又、温泉水以外の従来技術分野では例えば脱炭酸塔設備で散水により溶存ガスを分離する装置は存在する。然し温泉水に含まれるガス分離及び拡散を目的とする技術分野では該当する装置が存在しなかった。   Moreover, in the prior art fields other than hot spring water, for example, there exists an apparatus for separating dissolved gas by watering in a decarbonation tower facility. However, there is no corresponding device in the technical field for the purpose of gas separation and diffusion contained in hot spring water.

温泉水のガス分離技術分野で散水によるガス分離装置が存在しなかった背景として以下の3つの問題があった。第一に温泉水を空気中に散水すると空気中の酸素が温泉水に溶解し成分が酸化されること、又は温泉水中に溶解する二酸化炭素が空気中に放出されることにより二酸化炭素が排出されることによる炭酸水素イオンの減少に伴う化学変化が発生し、これら含有成分の変質により水への溶解度が低い成分が生成され当該発生物質が装置内に付着し当該付着物の除去費用がかかるという温泉スケール問題があった。第二に散水により温泉水の熱が放出され湯温が降下し降下分の加温のための燃料が増加するという問題があった。第三にガス分離に伴い装置内空気中に温泉水から水蒸気が供給され装置内空気が排気口から外気へ排出される際に気温の低い外気と接触し排気温の低下に伴って飽和水蒸気量が下がり過飽和した水蒸気が液化し白煙が発生する問題があった。発明が解決しようとする課題はこれら3つの副作用を防止又は抑制しつつ効率的且つ効果的なガス分離、拡散及び希釈を実施できる装置を実現することである。   In the field of gas separation technology for hot spring water, there were the following three problems as the background of the absence of gas separation devices by watering. First, when hot spring water is sprinkled into the air, oxygen in the air dissolves in the hot spring water and the components are oxidized, or carbon dioxide dissolved in the hot spring water is released into the air, so that carbon dioxide is discharged. The chemical change accompanying the reduction of hydrogen carbonate ion due to the occurrence of this, the component of the content of the component is low, the low solubility in water is generated, the generated material adheres in the equipment, and the removal cost of the deposit There was a hot spring scale problem. Secondly, there was a problem that the heat of the hot spring water was released by watering, the temperature of the hot water dropped, and the fuel for warming up the descent increased. Third, when water vapor is supplied from the hot spring water to the air inside the device due to gas separation and the air inside the device is discharged from the exhaust port to the outside air, it comes into contact with the outside air at a low temperature and the saturated water vapor amount as the exhaust temperature decreases However, there was a problem that the supersaturated water vapor liquefied and white smoke was generated. The problem to be solved by the invention is to realize an apparatus capable of performing efficient and effective gas separation, diffusion and dilution while preventing or suppressing these three side effects.

本発明の装置は、気体の水への溶解量は溶解する気体の圧力に比例するというヘンリーの法則を応用したもので温泉水を温泉井戸から汲み上げて本装置に送湯し装置内で高圧下にあった温泉井戸内の温泉水圧を降下させることにより、それに比例して分離対象ガスの気体圧力が下がることで分離対象ガスの溶解量が小さくなり、温泉水に溶解できなくなった分離対象ガスが自然放出する現象を利用してガス分離する。   The apparatus of the present invention is an application of Henry's law that the amount of gas dissolved in water is proportional to the pressure of the dissolved gas. The hot spring water is pumped from the hot spring well and supplied to the apparatus under high pressure. By reducing the hot spring water pressure in the hot spring well, the gas pressure of the gas to be separated decreases proportionally, so that the amount of gas to be separated decreases, and the gas to be separated that cannot be dissolved in the hot spring water. Gas separation is performed by utilizing the phenomenon of spontaneous release.

然し上記の装置では、外気との接触面積が小さいがゆえにガス分離が抑制されるため外気との接触面積を増加し分離対象ガスの分離を促進する必要があった。そこで本装置は散水管により温泉水を散水しシャワー状とし温泉水と装置内の空気との気液界面表面積を増加させるとともに散水管の下部に衝撃版を設置し温泉水に衝撃を与えることでヘンリーの法則による水中から装置内空気への分離対象ガス成分の移動を促進する。   However, in the above apparatus, since the gas contact is suppressed because the contact area with the outside air is small, it is necessary to increase the contact area with the outside air and promote the separation of the separation target gas. Therefore, this device is made by sprinkling hot spring water with a sprinkler tube to make it shower-like, increasing the gas-liquid interface surface area between the hot spring water and the air in the device, and installing an impact plate at the bottom of the sprinkler tube to impact the hot spring water. The movement of the gas component to be separated from underwater to the air in the apparatus according to Henry's law is promoted.

然し上記の装置では、水中の対象気体の分圧は接触する気体中の対象気体の分圧に比例するというヘンリーの法則により、装置内で分離対象ガスを分離した温泉水中の分離対象ガス濃度が装置内空気の分離対象ガス濃度と平衡し温泉水中の分離対象ガスの濃度がそれ以上は下がらなくなるため装置内空気中の分離対象ガス成分の分圧を下げる必要があった。そこで本装置は送風機を付属し装置内に外気を送風することで装置内の分離対象ガスの装置内空気中の分圧を降下させ分離を促進する。   However, according to Henry's law that the partial pressure of the target gas in the water is proportional to the partial pressure of the target gas in the contacting gas, the concentration of the separation target gas in the hot spring water that separated the separation target gas in the device is It was necessary to lower the partial pressure of the gas component to be separated in the air in the apparatus because the concentration of the gas to be separated in the hot spring water was not lowered any more because it was balanced with the concentration of the gas to be separated in the air in the apparatus. Therefore, the present apparatus is attached with a blower and blows outside air into the apparatus, thereby reducing the partial pressure in the apparatus air of the gas to be separated in the apparatus and promoting the separation.

然し上記の装置では、散水又は送風もしくはその両方により酸素を温泉水に供給し温泉水中の成分が酸化されること又は分離対象ガス成分ではない二酸化炭素等のガス成分が分離され炭酸水素イオン等の成分が減少し炭酸イオン等に変化することにより温泉水中の成分が変質し難溶性の化学物質が生成する温泉スケールが発生すること、及び温泉水に外気を送風し排気することにより温泉水の熱が排気に移動し排出され温泉水の湯温が下がることが起こり、これら副作用を抑制又は防止する必要があった。そこで本装置は散水の落差と送風量を調整することで温泉スケールの発生を抑制又は防止しつつ分離対象ガスの分離を促進するとともに温泉水の湯温の降下を抑制又は防止する。   However, in the above apparatus, oxygen is supplied to the hot spring water by sprinkling and / or air blowing, and the components in the hot spring water are oxidized, or the gas components such as carbon dioxide which is not the separation target gas component are separated and hydrogen carbonate ions and the like are separated. The hot spring water is generated by reducing the components and changing them to carbonate ions, etc., resulting in a hot spring scale in which the components in the hot spring water are altered and sparingly soluble chemical substances are generated, and the hot spring water is blown out and exhausted. Moved to the exhaust and discharged, and the temperature of the hot spring water dropped, and it was necessary to suppress or prevent these side effects. Therefore, the present apparatus adjusts the drop of the water spray and the amount of air blown to suppress or prevent the generation of the hot spring scale while promoting the separation of the separation target gas and suppressing or preventing the decrease in the hot water temperature.

然し上記の装置では、送風量の制限によりメタンなど可燃性ガスの場合は爆発の危険性、又は硫化水素のようなガスの場合は毒性が保持され危険となるため装置内空気の希釈を行う必要があった。そこで本装置は送風を二段階以上とし第一段階は分離対象ガスの温泉水中からの分離に必要な量を送風し、第二段階以後は装置内空気中の分離対象ガス濃度を爆発限界又は毒性限界から十分な安全率を設定した濃度まで装置内空気を希釈することで危険を防止又は抑制する。   However, in the above devices, the air inside the device needs to be diluted because of the limited risk of explosion due to the restriction of the amount of air blown in the case of flammable gases such as methane, or in the case of gases such as hydrogen sulfide. was there. Therefore, this equipment blows air in two or more stages, the first stage blows the amount necessary for separation of the separation target gas from the hot spring water, and after the second stage, the concentration of the separation target gas in the air in the apparatus is set to the explosion limit or toxicity. The danger is prevented or suppressed by diluting the air in the apparatus from the limit to a concentration that sets a sufficient safety factor.

然し上記の装置では、温泉水と送風空気の接触により分離対象ガスが放出されるに付随して温度の高い温泉水から相対的に温度の低い送風空気に熱が移動し、送風空気の気温が上昇し、その結果、相対的に湿度が下がり飽和水蒸気量が上がり、温泉水から送風空気に水蒸気が供給され、その後、排気口で外気に接触する際に排気温が外気に対して相対的に高いため、熱が排気から外気に移動し、排気温が下がり、それに比して飽和水蒸気量が下がり水蒸気が過飽和となり液化し白煙が発生するため、その抑制又は防止を行う必要があった。そこで本装置は水分除去部を有し水分除去するともに二次外気取り入れにより排気温を下げることで外気との接触の際に水蒸気が液化して白煙や霧となることを防止又は抑制する。   However, in the above device, heat is transferred from the hot spring water having a high temperature to the blowing air having a relatively low temperature as the separation target gas is released by the contact between the hot spring water and the blowing air, and the temperature of the blowing air is reduced. As a result, the humidity decreases and the amount of saturated water vapor increases, water vapor is supplied from the hot spring water to the blown air, and then the exhaust temperature is relatively relative to the outside air when contacting the outside air at the exhaust port. Since it is high, heat moves from the exhaust gas to the outside air, the exhaust gas temperature decreases, the amount of saturated water vapor decreases, the water vapor becomes supersaturated, liquefies and white smoke is generated, and it is necessary to suppress or prevent it. Therefore, the present apparatus has a moisture removing unit and removes moisture and lowers the exhaust temperature by taking in the secondary outside air, thereby preventing or suppressing the water vapor from being liquefied into white smoke or mist upon contact with the outside air.

然し上記の装置では、散水部、一次外気の取り入れ部、水分低減部、二次外気取り入れ部及び排気口を鉛直方向に縦積みすると装置高が大きくなり設置位置の制限を受け周囲に威圧感を与え景観を損なうため機械高さを抑制する必要があった。そこで本装置は横方向にも装置構造を展開し装置高を小さくする。   However, in the above device, when the water sprinkling unit, primary outside air intake unit, moisture reducing unit, secondary outside air intake unit and exhaust port are stacked vertically, the height of the device becomes large and the installation position is restricted, so that the surroundings are intimidating. It was necessary to suppress the machine height to damage the given landscape. Therefore, this apparatus expands the apparatus structure in the lateral direction to reduce the apparatus height.

然し上記の装置では、処理された温泉水に極微量に存在する分離対象ガスが処理済みの温泉水を貯留する部分の上空空間中に放出され滞留するためこの部分での滞留を防止する必要があった。そこで本装置は温泉貯留部の排気を行って分離対象ガスを温泉貯留部の上部から排出する。   However, in the above-described apparatus, it is necessary to prevent stagnation in this portion because the gas to be separated, which is present in a very small amount in the treated hot spring water, is released and stays in the upper space where the treated hot spring water is stored. there were. Therefore, this apparatus exhausts the hot spring storage part and discharges the separation target gas from the upper part of the hot spring storage part.

本発明によれば、温泉水から安全にガス分離、拡散及び希釈を効率的且つ効果的に行うことができ、副作用として発生する温泉水温の低下、温泉スケールの発生及び白煙の発生を防止又は抑制できるとともに可燃性ガスの爆発を防止又は抑制し有毒ガスの有害性を低減できる。又、その構造が強固であり操作も簡便で装置の清掃を容易とする構造となっており維持管理の手間も少ない。   According to the present invention, gas separation, diffusion, and dilution can be performed safely and effectively from hot spring water, and it is possible to prevent a decrease in hot spring water temperature that occurs as a side effect, generation of hot spring scale, and generation of white smoke. In addition to being able to suppress, explosion of flammable gas can be prevented or suppressed, and the toxicity of toxic gas can be reduced. In addition, the structure is strong, the operation is simple, and the apparatus is easy to clean.

図1において1は温泉水散水部及びガス分離拡散部で101の送湯管により送湯される分離対象ガスを含んだ温泉水を107の散水管で散水し108の衝撃版に衝突させ分離対象ガスを分離するとともに分離対象ガスを装置内空気へ拡散する。102の送風機により103の一次外気送風管を通じて一次外気を1に送風し分離対象ガス濃度が高まった装置内空気を5の落水部の上部を通過し送風方向を180度曲げて2の水分低減部へ上昇させる。この送風により装置内空気の分離対象ガス濃度が低くなり分離対象ガスの分離が促進される。2は装置内空気中の水分を低減するとともに102の送風機により104の二次外気送風管を通じて二次外気を取り入れ装置内空気中の分離対象ガス濃度を安全な濃度まで希釈すると同時に装置内空気の温度を外気温に近づける。3は消音部で排気音及び塔内のシャワー音を減衰し105のガス濃度検知器で装置内空気の分離対象ガス濃度を検知し運転管理を行い4の排気口へ送る。4は装置内空気を大気へ排出する。一方、1で分離処理された温泉水は5の落水部に落水する。5は1により分離対象ガスが分離された温泉水の落水を受けて6の温泉貯留部へ送る。6は106の配湯管により温泉水利用施設へ配湯されるまで温泉水を貯留する。101は温泉井戸から1への送湯管である。102は送風機である。103は一次外気送風管で1へ送風する。104は二次外気送風管で2へ送風する。105はガス濃度検知器である。106は温泉水利用施設への配湯管である。107は散水管で温泉水を散水する。108は衝撃版で散水された温泉水から衝撃によりガスを分離する。109は水位計で温泉水の水位を計測し水槽の貯留量管理をする。110は制御盤でガス濃度及び水槽内水位により運転管理をする。111は温泉井戸である。112はポンプで温泉水を揚湯する。113は流量センサで温泉供給量を管理する。114は吸気管で温泉水中に残留するガスが分離され滞留する6の温泉貯留部の上空からガスを排出する。   In FIG. 1, reference numeral 1 denotes a hot spring water sprinkling section and a gas separation / diffusion section containing hot spring water containing a gas to be separated fed by a hot water feeding pipe 101 through a sprinkling pipe 107 and colliding with an impact plate 108 to be separated. The gas is separated and the separation target gas is diffused into the air in the apparatus. The primary air is blown to 1 through the primary outside air blow pipe of 103 by the blower of 102, and the air in the apparatus in which the concentration of the separation target gas is increased passes through the upper part of the water falling part of 5 and the air blowing direction is bent by 180 degrees to 2 of the moisture reducing part To rise. By this blowing, the separation target gas concentration of the air in the apparatus is lowered, and the separation of the separation target gas is promoted. 2 reduces the moisture in the air inside the apparatus and takes in the secondary outside air through the secondary outside air blowing pipe 104 by the blower 102 to dilute the concentration of the separation target gas in the apparatus air to a safe concentration and at the same time Bring the temperature closer to the outside temperature. 3 is a muffler that attenuates exhaust sound and shower sound in the tower, and a gas concentration detector 105 detects the concentration of gas to be separated in the apparatus air, performs operation management, and sends it to the exhaust port 4. 4 discharges the air in the apparatus to the atmosphere. On the other hand, the hot spring water separated in 1 falls into 5 falling portions. 5 receives the fall of the hot spring water from which the separation target gas has been separated by 1 and sends it to the 6 hot spring storage section. 6 stores hot spring water by hot water supply pipes 106 until hot water is distributed to a hot spring water use facility. 101 is a hot water supply pipe from the hot spring well to 1. Reference numeral 102 denotes a blower. Reference numeral 103 denotes a primary outside air blowing pipe which blows air to 1. Reference numeral 104 denotes a secondary outside air blowing pipe for blowing air to 2. Reference numeral 105 denotes a gas concentration detector. 106 is a hot water pipe to a hot spring water utilization facility. Reference numeral 107 is a watering pipe for sprinkling hot spring water. 108 isolate | separates gas by the impact from the hot spring water sprinkled with the impact version. A water level gauge 109 measures the water level of the hot spring water and manages the amount of water stored in the water tank. 110 is a control panel that manages the operation according to the gas concentration and the water level in the water tank. 111 is a hot spring well. 112 pumps hot spring water with a pump. Reference numeral 113 denotes a flow rate sensor for managing the hot spring supply amount. Reference numeral 114 denotes an intake pipe that discharges gas from above the six hot spring storage portions where gas remaining in the hot spring water is separated and retained.

装置高を小さくするため1、2、3及び4の順序で縦積みせず、図1のように水平2列とする。1の温泉水散水部及びガス分離拡散部で鉛直下向きに送風し、5の落水部で送風された空気の流れを180度曲げて鉛直上向きに送風方向を変え、2を通過した後、90度曲げて3を通過し、90度曲げて4へ排気するという送風の流れとする。   In order to reduce the height of the apparatus, do not stack vertically in the order of 1, 2, 3 and 4, but use two horizontal rows as shown in FIG. 1 after hot spring water sprinkling section and gas separation / diffusion section are blown vertically downward, the flow of air blown by 5 falling water section is bent 180 degrees, the blowing direction is changed vertically upward, and after passing 2, 90 degrees It is assumed that the air flow is such that the air passes through 3 and is bent 90 degrees and is exhausted to 4.

この発明に係る温泉水のガス分離装置の実施例を挙げることにより、一層明確なものとする。但し、この発明は以下の実施例により何ら限定されるものではない。図2の正面図及び図3の側面図に本発明を温泉水のメタンガス分離装置として実施した事例を示す。図2の正面図では1の温泉水散水部及びガス分離拡散部と2の水分低減部の位置関係、又、103の一次外気送風管と104の二次外気送風管の位置関係が定かでないため図3の側面図で示した。本実施例では101の送湯管で最大150リットル毎分の温泉水を装置内に送る一方、102の送風機により送風される最大17立方メートル毎分の半分8.5立方メートルの外気を、103の一次外気送風管を通して装置内に送風する。1の温泉水散水部及びガス分離拡散部では温泉水から84リットル毎分のメタンガスが分離され、8.5立方メートルの外気と混合することにより、1パーセント体積濃度以下に希釈する。当該温泉水及び送風空気は5の落水部に流され、5でメタンガスが分離処理された温泉水とメタンガスが含まれる送風空気とに分ける。メタンガスを含む送風空気は5の落水部上空で送風方向を180度曲げ2の水分低減部へと上昇する。2は水分を除去し104の二次外気送風管により8.5立方メートルの外気を送風し0.5パーセント体積濃度以下までメタンを希釈するとともに送風空気の温度を外気温に近づける。そして3の消音部で騒音が発生しないように消音し、又105のガス濃度検知器で0.5パーセント体積濃度を基準に計測し管理しながら、4の排出口から大気へ放出する。一方、1で処理された温泉水は5の落水部から6の温泉貯留部に移動し、利用施設へ送られる。6は106の配湯管により温泉利用施設へ配湯されるまで貯留する。101は温泉井戸から1への送湯管である。102は送風機である。103は一次外気送風管で102の送風機により外気をとりいれ1へ送風する。104は二次外気送風管で102の送風機により外気をとりいれ2へ送風する。105はガス濃度検知器である。106は温泉水利用施設への配湯管である。114は吸気管で102の送風機により吸気を行い6の温泉貯留部上空に滞留したガスを排気する。   It will be made clearer by giving examples of the gas separator for hot spring water according to the present invention. However, this invention is not limited at all by the following examples. The front view of FIG. 2 and the side view of FIG. 3 show an example in which the present invention is implemented as a methane gas separator for hot spring water. In the front view of FIG. 2, the positional relationship between the hot spring water sprinkling part 1 and the gas separation / diffusion part 1 and the moisture reduction part 2 and the positional relation between the primary outside air blowing pipe 103 and the secondary outside air blowing pipe 104 are not clear. This is shown in the side view of FIG. In this embodiment, hot water of a maximum of 150 liters per minute is sent into the apparatus through 101 hot water supply pipes, while a maximum of 8.5 cubic meters of outside air blown by a blower of 102 is half of the primary air of 103. The air is blown into the apparatus through the outside air blowing pipe. In the hot spring water sprinkling part and the gas separation / diffusion part, methane gas of 84 liters per minute is separated from the hot spring water, and is diluted to 1% volume concentration or less by mixing with 8.5 cubic meters of outside air. The hot spring water and the blown air are allowed to flow through the water falling part 5 and are divided into the hot spring water in which the methane gas is separated and the blown air containing the methane gas. The blown air containing methane gas rises to the moisture reducing part of 2 by bending the blowing direction 180 degrees above the 5 falling part. 2 removes moisture and blows 8.5 cubic meters of outside air through the secondary outside air blowing pipe 104 to dilute methane to 0.5% volume concentration or less and bring the temperature of the blowing air closer to the outside air temperature. Then, the sound is silenced so that no noise is generated at the muffler 3, and is discharged from the 4 outlets to the atmosphere while being measured and managed with a gas concentration detector 105 based on the 0.5 percent volume concentration. On the other hand, the hot spring water treated in 1 moves from 5 falling water parts to 6 hot spring storage parts and is sent to the use facility. 6 is stored until hot water is distributed to hot spring use facilities by 106 hot water distribution pipes. 101 is a hot water supply pipe from the hot spring well to 1. Reference numeral 102 denotes a blower. Reference numeral 103 denotes a primary outside air blowing pipe which takes in outside air by a blower 102 and blows air to the air. Reference numeral 104 denotes a secondary outside air blower pipe which takes in outside air by the blower 102 and blows it to the air 2. Reference numeral 105 denotes a gas concentration detector. 106 is a hot water pipe to a hot spring water utilization facility. Reference numeral 114 denotes an intake pipe which sucks air from the blower 102 and exhausts the gas remaining in the hot spring storage section 6.

本発明の概念図である。It is a conceptual diagram of this invention. 本発明の実施事例の正面図である。It is a front view of the implementation example of this invention. 本発明の実施事例の側面図である。It is a side view of the implementation example of this invention.

符号の説明Explanation of symbols

1 温泉水散水部及びガス分離拡散部
2 水分低減部
3 消音部
4 排気口
5 落水部
6 温泉貯留部
101 送湯管
102 送風機
103 一次外気送風管
104 二次外気送風管
105 ガス濃度検知器
106 配湯管
107 散水管
108 衝撃版
109 水位計
110 制御盤
111 温泉井戸
112 ポンプ
113 流量センサ
114 吸気管
DESCRIPTION OF SYMBOLS 1 Hot spring water sprinkling part and gas separation / diffusion part 2 Moisture reduction part 3 Silencer part 4 Exhaust port 5 Water fall part 6 Hot spring storage part 101 Hot water supply pipe 102 Blower 103 Primary outside air ventilation pipe 104 Secondary outside air ventilation pipe 105 Gas concentration detector 106 Water distribution pipe 107 Sprinkling pipe 108 Impact plate 109 Water level gauge 110 Control panel 111 Hot spring well 112 Pump 113 Flow rate sensor 114 Intake pipe

Claims (3)

散水又は衝撃若しくはその両方によりガスを分離又は拡散若しくはその両方の機能を有することを特徴とする温泉水のガス分離装置 Gas separation apparatus for hot spring water, which has a function of separating and / or diffusing gas by watering or impact or both 送風機を有し一段階での送風又は二段階以上での送風をすることを特徴とする請求項第1項の温泉水のガス分離装置 A gas separator for hot spring water according to claim 1, wherein the apparatus has a blower and blows air in one stage or blows in two or more stages. 水分低減部又は温泉貯留部の滞留ガス排出部若しくはその両方を有することを特徴とする請求項第2項の温泉水のガス分離装置 The gas separator for hot spring water according to claim 2, comprising a moisture reducing section or a staying gas discharge section of the hot spring storage section, or both.
JP2008148886A 2008-06-06 2008-06-06 Spa-water gas separator Pending JP2009291729A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010279918A (en) * 2009-06-05 2010-12-16 Japan Aqua Tec Co Ltd Gas separation apparatus
JP2014163122A (en) * 2013-02-26 2014-09-08 Chinetsu World Kogyo Co Ltd Hot spring air blowout drainage silencer
JP2015058377A (en) * 2013-09-18 2015-03-30 地熱ワールド工業株式会社 Open system bubbling type methane gas removing mechanism
JP2018509296A (en) * 2015-05-18 2018-04-05 青島双瑞海洋環境工程股▲ふん▼有限公司 Hydrogen removal tank and ballast water treatment system having the same
JP2019034294A (en) * 2017-08-15 2019-03-07 シェルタッチ工業有限会社 Defoaming nozzle and liquid injection means
US10781112B2 (en) 2015-05-18 2020-09-22 Sunrui Marine Environment Engineering Co., Ltd. Dehydrogenation tank and ballast water treatment system having the same

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010279918A (en) * 2009-06-05 2010-12-16 Japan Aqua Tec Co Ltd Gas separation apparatus
JP2014163122A (en) * 2013-02-26 2014-09-08 Chinetsu World Kogyo Co Ltd Hot spring air blowout drainage silencer
JP2015058377A (en) * 2013-09-18 2015-03-30 地熱ワールド工業株式会社 Open system bubbling type methane gas removing mechanism
JP2018509296A (en) * 2015-05-18 2018-04-05 青島双瑞海洋環境工程股▲ふん▼有限公司 Hydrogen removal tank and ballast water treatment system having the same
US10781112B2 (en) 2015-05-18 2020-09-22 Sunrui Marine Environment Engineering Co., Ltd. Dehydrogenation tank and ballast water treatment system having the same
JP2019034294A (en) * 2017-08-15 2019-03-07 シェルタッチ工業有限会社 Defoaming nozzle and liquid injection means

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