JP2006187683A - Neutralization treatment device for waste water after washing of dialysis apparatus - Google Patents

Neutralization treatment device for waste water after washing of dialysis apparatus Download PDF

Info

Publication number
JP2006187683A
JP2006187683A JP2004382009A JP2004382009A JP2006187683A JP 2006187683 A JP2006187683 A JP 2006187683A JP 2004382009 A JP2004382009 A JP 2004382009A JP 2004382009 A JP2004382009 A JP 2004382009A JP 2006187683 A JP2006187683 A JP 2006187683A
Authority
JP
Japan
Prior art keywords
pipe
tower
washing
waste water
liquid
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.)
Granted
Application number
JP2004382009A
Other languages
Japanese (ja)
Other versions
JP4643254B2 (en
Inventor
Setsuo Kobayashi
節夫 小林
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2004382009A priority Critical patent/JP4643254B2/en
Publication of JP2006187683A publication Critical patent/JP2006187683A/en
Application granted granted Critical
Publication of JP4643254B2 publication Critical patent/JP4643254B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • External Artificial Organs (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a neutralization treatment device for waste water after the washing of a dialysis apparatus which can deal with enlargement though being a relatively simple structure, is easily maintainable, reduces the unneeded consumption of a neutralizer, and can stably and securely perform treatment for waste water after the washing of a dialysis apparatus. <P>SOLUTION: The neutralization treatment device comprises: a tower body 1 where the lower part 1a in the tower is provided with a drainboard 11 for dewatering, the tower bottom part 1b at the lower part of the drainboard 11 is provided with a liquid outflow tube 12, and the upper part 1c of the tower is provided with a liquid distributor 14 of sprinkling waste water 6 after the washing of a dialysis apparatus; and a solid neutralizer 2 as granular matter dissolved in water, exhibiting acidity or alkalinity and packed onto the drainboard 11. The waste water 6 after the washing of the dialysis apparatus is sprinkled from the liquid distributor 14 so as to wet the neutralizer 2 and is made to flow down, and, by the dissolution of the neutralizer 2, neutralization treatment is performed. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は透析機器類の消毒,洗浄排水のpHを中性にする透析機器洗浄排水の中和処理装置に関する。   The present invention relates to a dialysis machine cleaning wastewater neutralizing apparatus for neutralizing the pH of dialysis equipment and cleaning wastewater.

人工透析を行う病院,診療所等では透析終了後に、例えば水洗−酸洗浄−水洗−薬洗−水洗といった工程を経る透析機器の消毒,洗浄がなされる。酸洗浄には酢酸などの酸性洗浄水が、薬洗には次亜塩素酸ナトリウムなどのアルカリ洗浄水が用いられる。これに伴って酸性に傾いた洗浄排水やアルカリ性に傾いた洗浄排水が排出される。
また、病院,診療所等によっては酢酸などの酸洗浄のみによる殺菌洗浄も行われ、これに伴い酸性に傾いた洗浄排水が排出される。該透析機器洗浄排水は水質基準内に収まっていないため、中和処理してから下水道へ流されることとなる。本出願人はこの酸性に傾いた透析機器洗浄排水を中和処理する装置を先に提案した(特許文献1参照)。
In hospitals, clinics, and the like where artificial dialysis is performed, dialysis equipment is sterilized and washed through processes such as water washing, acid washing, water washing, drug washing, and water washing after the completion of dialysis. Acid cleaning water such as acetic acid is used for the acid cleaning, and alkaline cleaning water such as sodium hypochlorite is used for the chemical cleaning. Along with this, washing wastewater inclined to acidity and washing wastewater inclined to alkalinity are discharged.
In some hospitals, clinics, etc., sterilization cleaning is performed only by acid cleaning such as acetic acid, and accordingly, waste water that is inclined toward acidity is discharged. Since the dialysis machine washing wastewater does not fall within the water quality standard, it is discharged to the sewer after neutralization. The present applicant has previously proposed a device for neutralizing the dialysis machine washing wastewater inclined to acidity (see Patent Document 1).

特開2002−282869公報JP 2002-282869 A

しかるに、特開2002−282869公報技術(従来技術1)には次のような問題があった。
透析機器洗浄排水の配管途中のラインに半円筒形のpH調節機を組み込んでいるので、20床程度のベッド数の比較的小規模の病院向けに限られていた。ベッド数の増加と共に配管途中に収めるのが困難になると共に、中和処理が不十分になるときがあった。配管を流れる実際の透析機器洗浄排水は流量,流速が常に変動している。該洗浄排水の流量が少ない場合は配管壁面をつたって流れ落ちることが多く、流量が多くなっても配管内を充満しているケースはともかく、充満してない場合は偏流する傾向にある。pH調節機に至るまでの排水経路がいくつも分岐していたりしているのが原因と考えられるが、そもそもベッド数増加のスケールアップ化が偏流を生まれ易くしている。上階から下階へ垂直配設される透析機器の洗浄排水用配管の途中にpH調節機を設けても、該洗浄排水が偏流状態でpH調節機内を流下するため、所定の効果を得にくく、また固形pH調節剤たる中和剤も均等に消耗しないで不必要に消費量が多くなることがあった。
さらに透析機器の洗浄排水用配管途中に設けられることから、時としてpH調節機内に透析機器洗浄排水が溜まったまま放置される場合があり、透析機器洗浄排水に浸かったままの固形中和剤を溶解させやせ細らせていた。
However, the technique disclosed in Japanese Patent Laid-Open No. 2002-282869 (Prior Art 1) has the following problems.
Since a semi-cylindrical pH controller is incorporated in a line in the middle of the dialysis machine washing and drainage pipe, it has been limited to relatively small hospitals having about 20 beds. As the number of beds increased, it became difficult to fit in the middle of the piping, and the neutralization treatment was sometimes insufficient. The flow rate and flow velocity of the actual dialysis machine washing wastewater flowing through the pipe always fluctuate. When the flow rate of the washing wastewater is small, it often flows down along the wall surface of the pipe, and even if the flow rate is high, the pipe is filled, and when it is not full, it tends to drift. This may be due to the fact that the drainage route leading to the pH controller is branched, but in the first place, the increase in the number of beds makes it easier to create a drift. Even if a pH adjuster is installed in the middle of the washing drainage pipe of a dialysis machine that is vertically arranged from the upper floor to the lower floor, the washing wastewater flows down in the pH controller in a drift state, so that it is difficult to obtain a predetermined effect. Further, the neutralizing agent as a solid pH adjusting agent may not be consumed evenly, and the consumption may be increased unnecessarily.
Furthermore, since it is installed in the middle of the dialysis machine washing drainage pipe, the dialysis machine washing effluent may sometimes be left in the pH adjuster. It was dissolved and thinned.

本発明は上記問題点を解決するもので、比較的簡単な構造ながら大型化に対応でき、維持管理も容易で、中和剤の不必要な消耗を減らし、透析機器の洗浄排水を安定的に且つ確実に排水処理できる透析機器洗浄排水の中和処理装置を提供することを目的とする。   The present invention solves the above-mentioned problems, can cope with an increase in size with a relatively simple structure, is easy to maintain, reduces unnecessary consumption of the neutralizing agent, and stably discharges washing water from dialysis equipment. It is another object of the present invention to provide a neutralization treatment apparatus for dialysis equipment washing waste water that can reliably treat waste water.

前記目的を達成すべく、請求項1に記載の発明の要旨は、塔内の下部に水切り用簀子板を設け、該簀子板の下方の塔底部に液流出管を設けると共に、塔上部に透析機器の洗浄排水を散水する液分布器を設けた塔本体(1)と、水に溶解して酸性又はアルカリ性を呈する粒状物にして、前記簀子板上に充填される固形の中和剤(2)と、を具備し、該中和剤を濡らすように前記液分布器から透析機器の洗浄排水を散水して流下させ、該中和剤の溶解により中和処理をなすことを特徴とする透析機器洗浄排水の中和処理装置にある。
請求項2に記載の発明の要旨は、塔内の下部に水切り用簀子板を設け、該簀子板の下方の塔底部に液流出管を設けると共に、塔上部に透析機器の洗浄排水を散水する液分布器を設けた塔本体(1)と、水に溶解してアルカリ性を呈する粒状物にして、前記簀子板上に充填される固形の中和剤(2)と、透析機器の洗浄排水用本管の途中に設けられる開閉弁(3)と、該開閉弁よりも上流側の前記本管から略水平又は下降傾斜して分岐し前記液分布器へ導く上流側分岐管(4)と、前記液流出管から水平又は下降傾斜して前記開閉弁よりも下流側の前記本管へと接続する下流側分岐管(5)、又は前記液流出管から略水平又は下降傾斜して雑排水管へと接続する下流側分岐管(5)と、を具備し、前記中和剤を濡らすように前記液分布器から透析機器の洗浄排水を散水して流下させ、該中和剤の溶解により中和処理をなすことを特徴とする透析機器洗浄排水の中和処理装置にある。
請求項3の発明たる透析機器洗浄排水の中和処理装置は、請求項2で、中和剤が水酸化マグネシウム又は酸化マグネシウムを主成分とする粒状物からなり、且つ前記液分布器がパイプの下面側に透孔を多数形成した液分配管からなることを特徴とする。
請求項4の発明たる透析機器洗浄排水の中和処理装置は、請求項3で、塔本体の外形をその正面板の縦横長さに比べ奥行き幅が狭い略方形体に形成し、且つ該塔本体の外形の奥行き幅の略中間地点を一直線状に1本の前記液分配管が横断するよう配設されてなることを特徴とする。
In order to achieve the object, the gist of the invention described in claim 1 is that a draining insulator plate is provided at the lower part of the tower, a liquid outflow pipe is provided at the bottom of the tower, and a dialysis is provided at the upper part of the tower. A tower main body (1) provided with a liquid distributor for spraying the washing waste water of the equipment, and a solid neutralizing agent (2) which is dissolved in water and becomes acidic or alkaline and filled on the insulator plate. ), And the washing effluent of the dialysis device is sprinkled down from the liquid distributor so as to wet the neutralizing agent, and neutralization treatment is performed by dissolving the neutralizing agent. It is in the neutralization processing equipment of equipment washing wastewater.
The gist of the invention described in claim 2 is that a draining insulator plate is provided at the lower part of the tower, a liquid outflow pipe is provided at the bottom of the tower below the insulator plate, and washing waste water from the dialysis equipment is sprinkled at the upper part of the tower. A column main body (1) provided with a liquid distributor, a granular material which dissolves in water and exhibits alkalinity, is filled with a solid neutralizing agent (2) filled on the insulator plate, and is used for washing and draining dialysis equipment. An on-off valve (3) provided in the middle of the main pipe, an upstream branch pipe (4) branching from the main pipe upstream of the on-off valve substantially horizontally or downwardly and leading to the liquid distributor; A downstream branch pipe (5) connected to the main pipe downstream from the on-off valve with a horizontal or downward inclination from the liquid outflow pipe, or a miscellaneous drain pipe with a substantially horizontal or downward inclination from the liquid outflow pipe. A downstream branch pipe (5) connected to the dialysis device from the liquid distributor so as to wet the neutralizing agent. Water spray caused to flow down, in neutralization apparatus dialysis machine washing waste water, characterized in that forming the neutralized by the dissolution of said neutralizing agent.
A neutralization treatment apparatus for dialysis equipment washing wastewater according to a third aspect of the present invention is the neutralization treatment apparatus according to the second aspect, wherein the neutralizing agent is made of particulate matter mainly composed of magnesium hydroxide or magnesium oxide, and the liquid distributor is a pipe. It consists of a liquid distribution pipe in which a large number of through holes are formed on the lower surface side.
According to a fourth aspect of the present invention, there is provided a neutralization apparatus for washing effluent from dialysis equipment according to the third aspect, wherein the outer shape of the tower body is formed into a substantially rectangular shape having a narrower width than the length and width of the front plate. One liquid distribution pipe is disposed so as to cross a substantially intermediate point of the depth width of the outer shape of the main body in a straight line.

請求項1の発明のごとく、塔内の下部に水切り用簀子板を設け、該簀子板の下方の塔底部に液流出管を設けると共に、塔上部に透析機器の洗浄排水を散水する液分布器を設けた塔本体(1)と、水に溶解して酸性又はアルカリ性を呈する粒状物にして、前記簀子板上に充填される固形の中和剤(2)と、を具備し、該中和剤を濡らすように前記液分布器から透析機器の洗浄排水を散水して流下させ、該中和剤の溶解により中和処理をなすと、透析機器の洗浄排水管のラインから別個独立して塔本体を設置できるので、簡単な構造ながら透析機器の洗浄排水量が大なるものに対してもたやすく対応できる。また維持管理も楽に対応できる。中和剤は充填塔形式で簀子板上に充填され、該簀子板によって水切りされるので、中和剤の不必要な消耗を減らす。透析機器の洗浄排水を安定的に且つ確実に処理できる。
請求項2の発明のごとく、透析機器の洗浄排水用本管の途中に設けられる開閉弁(3)と、該開閉弁よりも上流側の前記本管から略水平又は下降傾斜して分岐し前記液分布器へ導く上流側分岐管(4)と、前記液流出管から水平又は下降傾斜して前記開閉弁よりも下流側の前記本管へと接続する下流側分岐管(5)、又は前記液流出管から略水平又は下降傾斜して雑排水管へと接続する下流側分岐管(5)と、を具備すると、重力落差を利用して透析機器の洗浄排水を簡単に処理できる。請求項3の発明のごとく、中和剤が水酸化マグネシウム又は酸化マグネシウムを主成分とする粒状物からなると、酸中和処理中にアクが出ず、且つ粒径も適度な大きさで、作業性,取扱いに優れたものとなる。前記液分布器がパイプの下面側に透孔を多数形成した液分配管からなると、液分布器がシンプルになる。請求項4の発明のごとく、塔本体の外形をその正面板の縦横長さに比べ奥行き幅が狭い略方形体に形成し、且つ該塔本体外形の奥行き幅の略中間地点を一直線状に1本の前記液分配管が横断するよう配設されると、中和処理装置の構造を簡素化できる。
As in the first aspect of the invention, a liquid distributor is provided with a draining insulator plate at the bottom of the tower, a liquid outflow pipe at the bottom of the tower below the insulator plate, and the washing effluent of dialysis equipment is sprinkled at the top of the tower. A column main body (1) provided with a solid neutralizing agent (2) which is dissolved in water and becomes acidic or alkaline and is packed on the insulator plate. If the neutralizing treatment is performed by dissolving the neutralizing agent by spraying the washing effluent of the dialysis device from the liquid distributor so as to wet the agent, and the neutralizing treatment is performed by dissolving the neutralizing agent, the column is separated from the washing drain pipe line of the dialysis device. Since the main body can be installed, it can easily cope with a large dialysis machine washing wastewater volume despite its simple structure. Maintenance can also be handled easily. The neutralizing agent is packed on the insulator plate in the form of a packed tower and drained by the insulator plate, thereby reducing unnecessary consumption of the neutralizing agent. Washing waste water from dialysis equipment can be treated stably and reliably.
As in the invention of claim 2, the on-off valve (3) provided in the middle of the washing and drainage main pipe of the dialysis machine and the main pipe on the upstream side of the on-off valve are branched substantially horizontally or downwardly and branched. An upstream branch pipe (4) leading to the liquid distributor, and a downstream branch pipe (5) connected to the main pipe downstream from the on-off valve by being inclined horizontally or downward from the liquid outlet pipe, or If the downstream branch pipe (5) connected to the miscellaneous drainage pipe at a substantially horizontal or downward inclination from the liquid outflow pipe is provided, the washing drainage of the dialysis machine can be easily treated using the gravity drop. As in the invention of claim 3, when the neutralizing agent is made of a granular material containing magnesium hydroxide or magnesium oxide as a main component, no ak is produced during the acid neutralization treatment, and the particle size is moderate. Excellent in handling and handling. If the liquid distributor is composed of a liquid pipe having a large number of through holes formed on the lower surface side of the pipe, the liquid distributor becomes simple. As in the invention of claim 4, the outer shape of the tower main body is formed into a substantially rectangular shape having a narrower depth width than the length and width of the front plate, and a substantially intermediate point of the depth width of the tower main body outer shape is aligned in a straight line. When the liquid distribution pipe of the book is arranged so as to cross, the structure of the neutralization processing device can be simplified.

本発明の透析機器洗浄排水の中和処理装置は、比較的簡単な構造にして透析機器の洗浄排水処理量が増えても容易に装置化でき、更に維持管理が楽で中和剤の不必要な消耗を減らし、加えて低コストで透析機器の洗浄排水を安定的に且つ確実に排水処理できるなどの優れた効果を発揮する。   The neutralization treatment apparatus for dialysis equipment washing wastewater of the present invention has a relatively simple structure and can be easily realized even if the washing effluent treatment amount of the dialysis equipment increases, further maintenance is easy, and no neutralizer is required. In addition, it is possible to reduce the amount of exhaustion, and at the same time, it exhibits excellent effects such as low-cost and stable and reliable drainage treatment of dialysis equipment.

以下、本発明に係る透析機器洗浄排水の中和処理装置(以下、単に「中和処理装置という。)について詳述する。図1〜図6は本発明の中和処理装置の一形態で、図1は透析機器の洗浄排水用本管に接続してなる中和処理装置の概略正面断面図、図2は図1の側面図、図3は(イ)が図1のI-I線矢視図で(ロ)が液分布器の横断面図で(ハ)が塔本体の上蓋周りの拡大図である。図4は上蓋を外した中和処理装置の平面図、図5は液分布器周りの拡大図、図6は図1〜図5と別態様の透析機器の洗浄排水用本管、雑排水管との接続例を示す中和処理装置の説明図である。尚、図5は液分散板の図示を省く。   Hereinafter, the neutralization treatment apparatus (hereinafter simply referred to as “neutralization treatment apparatus”) of dialysis equipment washing wastewater according to the present invention will be described in detail. FIGS. 1 to 6 are one embodiment of the neutralization treatment apparatus of the present invention. 1 is a schematic front cross-sectional view of a neutralization treatment apparatus connected to a main pipe for washing and draining dialysis equipment, FIG. 2 is a side view of FIG. 1, and FIG. 3 is a view taken along line II in FIG. (B) is a cross-sectional view of the liquid distributor, (c) is an enlarged view around the upper lid of the tower body, Fig. 4 is a plan view of the neutralization processing apparatus with the upper lid removed, and Fig. 5 is around the liquid distributor. Fig. 6 is an explanatory view of a neutralization treatment apparatus showing an example of connection between a main pipe for washing and drainage and a miscellaneous drain pipe of a dialysis machine according to another embodiment of Fig. 1 to Fig. 5. The illustration of the dispersion plate is omitted.

中和処理装置は塔本体1と中和剤2と開閉弁3と上流側分岐管4と下流側分岐管5とを備える(図1)。
塔本体1は塔内に中和剤2を充填して透析機器の洗浄排水6を中和処理する装置の本体部分である。正面板10aと背面板10bと側板10cと底板10dとで上面開口の有底筒状体に形成され、上面開口を上蓋10eで開閉自在にして塔本体1の外壁シェルが形成される。本実施形態は図3,図4のごとく塔本体1の外形をその正面板10aの縦横長さに比べ奥行き幅Wが狭い略方形体に形成する。底板10dは側面視が図3のごとく中央下部に向けてコーン状に狭まり、塔内に注がれた洗浄排水6が中央下部に集まるようにする。正面板10a,背面板10bの下縁は、スカート縁として該中央下部より下に延び、それらの下端部分にレベル調節具LTを取付けて、塔本体1が床GLに立設する。
The neutralization apparatus includes a tower body 1, a neutralizing agent 2, an on-off valve 3, an upstream branch pipe 4, and a downstream branch pipe 5 (FIG. 1).
The tower main body 1 is a main body portion of an apparatus for filling the tower with a neutralizing agent 2 and neutralizing the washing waste water 6 of the dialysis equipment. The front plate 10a, the back plate 10b, the side plate 10c, and the bottom plate 10d are formed into a bottomed cylindrical body having an upper surface opening, and the outer wall shell of the tower body 1 is formed by opening and closing the upper surface opening with an upper lid 10e. In the present embodiment, as shown in FIGS. 3 and 4, the outer shape of the tower body 1 is formed in a substantially rectangular shape having a narrower width W than the length and width of the front plate 10a. As shown in FIG. 3, the bottom plate 10d narrows in a cone shape toward the center lower portion as shown in FIG. The lower edges of the front panel 10a and the rear panel 10b extend below the center lower part as skirt edges, and the level adjuster LT is attached to their lower end parts, so that the tower body 1 stands on the floor GL.

該塔本体1に係る塔内の下部には水切り用簀子板11が設けられ、該簀子板11の下方の塔底部1bに液流出管12が設けられると共に、塔上部1cには透析機器の洗浄排水6を散水する液分布器14が設けられる。本実施形態は、さらに一側板10c寄りの塔内部で、該側板10cに沿って液分布器14から簀子板11に至る所まで仕切板10fが立設し、液分布器14から簀子板11に至る塔内は、該仕切板10fにより中和剤2が充填される室とオーバーフロー室とに区画化される。中和剤2が充填される室の横断面は、中和剤2の充填層が存在しても、透析機器の洗浄排水6が速やかに流下するに十分な断面積が確保される。尚、前記オーバーフロー室は、中和剤2が経時変化で透析機器洗浄排水6に溶解し小さくなったり不溶物で充填層に沈着したりして、充填層が目詰まり状態になる万一の場合に備えるものである。中和剤2の充填層が詰まってもオーバーフロー室に洗浄排水6をバイパスさせて対処できるようにする。
符号18は液分布器14の若干下方で塔内を横断敷設される多孔板からなる液分散板を示す。液分散板18は中和剤2が充填される室の方だけに設けられる。液分散板18は必要に応じ設けられる。該液分散板18を設けることによって、簀子板11上に充填される中和剤2に対し、液分布器14だけによる透析機器洗浄排水6の散水よりも一段と散水61の均等分配が進み、透析機器洗浄排水6の一層確実な中和処理をなす。符号19bは塔上部1cの内壁に固着する受部材で、液分散板18を支持する。
A draining insulator plate 11 is provided in the lower part of the tower according to the tower body 1, a liquid outflow pipe 12 is provided in a tower bottom 1b below the insulator plate 11, and a dialysis machine is washed in the tower upper part 1c. A liquid distributor 14 for spraying the drainage 6 is provided. In the present embodiment, a partition plate 10f is further erected from the liquid distributor 14 to the insulator plate 11 along the side plate 10c from the liquid distributor 14 to the insulator plate 11 inside the tower near the one side plate 10c. The inner tower is partitioned into a chamber filled with the neutralizing agent 2 and an overflow chamber by the partition plate 10f. The cross section of the chamber filled with the neutralizing agent 2 is ensured to have a sufficient cross-sectional area so that the washing waste water 6 of the dialysis machine can quickly flow down even if a packed bed of the neutralizing agent 2 exists. In the case of the overflow chamber, the neutralizing agent 2 is dissolved in the dialysis machine washing waste water 6 over time and becomes smaller or deposits in the packed bed with insoluble matter, so that the packed bed becomes clogged. To prepare for. Even if the packed bed of the neutralizing agent 2 is clogged, the washing drain 6 is bypassed to the overflow chamber so that it can be dealt with.
Reference numeral 18 denotes a liquid dispersion plate formed of a perforated plate that is laid across the tower slightly below the liquid distributor 14. The liquid dispersion plate 18 is provided only in the chamber filled with the neutralizing agent 2. The liquid dispersion plate 18 is provided as necessary. By providing the liquid dispersion plate 18, the uniform distribution of the water spray 61 further proceeds to the neutralizing agent 2 filled on the insulator plate 11 rather than the water spray of the dialysis equipment washing waste water 6 by the liquid distributor 14 alone. A more reliable neutralization treatment of the equipment cleaning waste water 6 is performed. Reference numeral 19b is a receiving member fixed to the inner wall of the tower upper part 1c, and supports the liquid dispersion plate 18.

透析機器の洗浄排水用本管9が図1のごとく塔本体1近くで垂直方向に配設されており、塔上部1c側寄りの高さの地点に開閉弁3が設けられる。そして、透析機器の洗浄排水用本管9の途中に設けられるこの開閉弁3よりも上流側に位置する本管9から上流側分岐管4が分岐して前記液分布器14とつながる。また、前記開閉弁3よりも下流側に位置する本管9から下流側分岐管5が分岐して前記液流出管12と接続する。上流側分岐管4は本管9から液分布器14へほぼ同レベルの高さでほぼ水平配設されるが、本管9から液分布器14へは透析機器洗浄排水6を流れ易くすべく下降傾斜をつけて配設するとより好ましくなる。下流側分岐管5は本管9から液流出管12へほぼ同レベルの高さでほぼ水平配設されるが、本管9から液流出管12へは透析機器洗浄排水6を流れ易くすべく上昇傾斜をつけて配設するとより好ましくなる。すなわち、下流側分岐管5は液流出管12から下降傾斜して開閉弁3よりも下流側の本管9へ接続することによって透析機器洗浄排水6が重力落差で円滑に流れ落ちる。尚、上流側分岐管4,下流側分岐管5は本管9から分岐するT型継手の所で、図1のごとく一旦立ち上がるようにする。開閉弁3が開のときに、透析機器洗浄排水6が不用意に中和処理装置の方へ流れ込まないようにするためである。符号92は本管ライン上で、上流側分岐管4が分岐する地点から開閉弁3までの上流側短管である。該短管は開閉弁3が閉のとき透析機器洗浄排水6が溜まる所になるので短くする方がよい。符号93は本管ライン上で、開閉弁3から下流側分岐管5が本管9に合流する地点までの下流側短管を示す。   As shown in FIG. 1, a main pipe 9 for washing and draining the dialysis machine is arranged in the vertical direction near the tower body 1, and the opening / closing valve 3 is provided at a point near the tower upper part 1 c side. Then, the upstream branch pipe 4 branches from the main pipe 9 located upstream of the on-off valve 3 provided in the middle of the washing / drain main pipe 9 of the dialysis machine and is connected to the liquid distributor 14. Further, the downstream branch pipe 5 branches from the main pipe 9 located on the downstream side of the on-off valve 3 and is connected to the liquid outflow pipe 12. The upstream side branch pipe 4 is disposed substantially horizontally from the main pipe 9 to the liquid distributor 14 at substantially the same level height, but in order to facilitate the flow of the dialysis device washing waste water 6 from the main pipe 9 to the liquid distributor 14. It is more preferable to arrange with a downward slope. The downstream branch pipe 5 is disposed substantially horizontally from the main pipe 9 to the liquid outflow pipe 12 at substantially the same level height, but in order to facilitate the flow of the dialysis device washing waste water 6 from the main pipe 9 to the liquid outflow pipe 12. It is more preferable to arrange with an upward slope. That is, the downstream branch pipe 5 is inclined downward from the liquid outflow pipe 12 and connected to the main pipe 9 on the downstream side of the on-off valve 3, so that the dialysis machine washing waste water 6 smoothly flows down due to a gravity drop. The upstream branch pipe 4 and the downstream branch pipe 5 are T-shaped joints that branch from the main pipe 9 and are once raised as shown in FIG. This is to prevent the dialysis machine washing waste water 6 from inadvertently flowing toward the neutralization apparatus when the on-off valve 3 is open. Reference numeral 92 denotes an upstream short pipe from the point where the upstream branch pipe 4 branches to the on-off valve 3 on the main line. Since the short pipe becomes a place where the dialysis machine washing waste water 6 is accumulated when the on-off valve 3 is closed, it is preferable to shorten the short pipe. Reference numeral 93 denotes a downstream short pipe from the on-off valve 3 to a point where the downstream branch pipe 5 joins the main pipe 9 on the main line.

前記簀子板11は多孔板や網の目状、或いは格子状として、水切りし得る通水性を有する平板状体又はグリッドである。ここでは金属製金網を平板状にした簀子板11とする。塔底部1bから所定高さの塔下部1aの内周壁に金属製角材からなる受部材19bを固着し、該受部材に支持されるようにして簀子板11が水平に載置される。簀子板11の篩の目は固形粒状物たる中和剤2を載せることのできる大きさにする。   The insulator plate 11 is a flat plate or grid having water permeability that can be drained in the form of a perforated plate, mesh, or lattice. Here, it is assumed that the metal wire mesh is a flat insulator plate 11. A receiving member 19b made of a metal square is fixed to the inner peripheral wall of the tower lower part 1a at a predetermined height from the tower bottom 1b, and the insulator plate 11 is placed horizontally so as to be supported by the receiving member. The size of the screen of the insulator plate 11 is set so that the neutralizing agent 2 as a solid granular material can be placed.

前記液流出管12は塔内と導通するようにして塔底部1bから外方に突出するノズルで、ここでは底板10dが形成する前記中央下部の高さレベルの塔本体1側板10cに固着される。液流出管12は透析機器洗浄排水6の本管9と略同径とする。符号12aは液流出管12の先端に設けたフランジを示す。フランジ結合で液流出管12は下流側分岐管5と連結して本管9とつながる。符号13は該液流出管12と対向する塔本体側板10cに設けられる下部ノズル、符号13aは下部ノズル13の先端に設けたフランジ、符号13bは盲フランジを示す。液流出管12と下部ノズル13が一直線上にあり、盲フランジ13bを外して定期点検,清掃等のメンテナンスがし易くなっている。   The liquid outflow pipe 12 is a nozzle that protrudes outward from the tower bottom 1b so as to be electrically connected to the inside of the tower, and is fixed to the tower main body 1 side plate 10c at the lower level in the center formed by the bottom plate 10d. . The liquid outflow pipe 12 has substantially the same diameter as the main pipe 9 of the dialysis machine washing drainage 6. Reference numeral 12 a denotes a flange provided at the tip of the liquid outflow pipe 12. The liquid outflow pipe 12 is connected to the downstream branch pipe 5 and connected to the main pipe 9 by flange connection. Reference numeral 13 denotes a lower nozzle provided on the tower body side plate 10c facing the liquid outflow pipe 12, reference numeral 13a denotes a flange provided at the tip of the lower nozzle 13, and reference numeral 13b denotes a blind flange. The liquid outflow pipe 12 and the lower nozzle 13 are in a straight line, and the blind flange 13b is removed to facilitate maintenance such as periodic inspection and cleaning.

前記液分布器14は塔上部1cに設けられる透析機器洗浄排水6の液分配器で、より詳しくは塔本体1内の簀子板11上に充填される中和剤2の充填層にその上から透析機器の洗浄排水6を分散させて注水し得る液分配器である。ここでの液分布器14は図3(ロ)のようにパイプの下面側に透孔141を多数形成した液分配管14aからなり、図1,図4のごとく塔本体1の奥行き幅Wの略中間地点を一直線状に1本の液分配管14aが横断するよう配設される。透孔141は中和剤2の充填層に略均等に散水できるようパイプ下面側に所定ピッチで設けられる。塔上部1cの側板10cから突設する液分配管14aに係る導入ノズル16は、その内端部分が塔内に収まる。また該導入ノズル16と対向する塔上部1cの側板10cに上部ノズル15が突設し、該上部ノズル15の内端部分が塔内に収まる。上部ノズル15の内端は仕切板10fを越え、中和剤2が充填される室内に達する。液分配管14aは図1のごとく両側板10c間の長さより若干小さめの管長で、導入ノズル16の内端と上部ノズル15の内端との間に嵌まる長さの透孔141付きパイプである。液分配管14aの両端をバンド締結することにより導入ノズル16,液分配管14a,上部ノズル15が一直線につながる。透析機器洗浄排水6の本管9の上流部91から上流側分岐管4,導入ノズル16を経て、液分配管14aに導かれた透析機器の洗浄排水6は透孔141から散水となって、雨だれのごとく降り落ちる(図5)。塔本体1の奥行き幅Wが狭いため、1本の液分配管14aを通すだけで中和剤2の充填層上面に略均等に透析機器洗浄排水6を散水できる。中和剤2を濡らすように前記液分布器14から透析機器洗浄排水6を散水して流下させ、該中和剤2の溶解により中和処理をなす。簀子板11が水切りとなって、散水,流下する透析機器洗浄排水6を流し去る。中和剤2が不必要に透析機器洗浄排水6に長時間浸からないので、中和剤2のやせ細りや過度の溶解が起こる虞はない。導入ノズル16,液分配管14a,上部ノズル15の管径は透析機器洗浄排水6の本管9の径と略同じとする。液分配管14aはパイプ径,パイプ長さを同じくして、透孔141の個数や大きさ、透孔141のピッチ配列等が違うタイプのものが適宜準備される。バンド17a,17bを外せば(図3のイの鎖線)、透孔141の個数や透孔141の大きさの異なる液分配管14aと容易に取り替えることができる。尚、液分配管14aはパイプを半割りにしてその半割り椀状部に透孔141を多数設けるものでもよい。   The liquid distributor 14 is a liquid distributor for the dialysis equipment washing waste water 6 provided in the upper part 1c of the tower, and more specifically, on the packed bed of the neutralizing agent 2 filled on the insulator plate 11 in the tower body 1 from above. This is a liquid distributor capable of dispersing and injecting washing waste water 6 of a dialysis machine. As shown in FIG. 3 (b), the liquid distributor 14 includes a liquid distribution pipe 14a in which a large number of through holes 141 are formed on the lower surface side of the pipe, and has a depth width W of the tower body 1 as shown in FIGS. One liquid distribution pipe 14a is arranged so as to cross a substantially intermediate point in a straight line. The through holes 141 are provided at a predetermined pitch on the lower surface side of the pipe so that the filling layer of the neutralizing agent 2 can be sprinkled substantially evenly. The inner end portion of the introduction nozzle 16 related to the liquid distribution pipe 14a protruding from the side plate 10c of the tower upper part 1c is accommodated in the tower. An upper nozzle 15 protrudes from the side plate 10c of the tower upper portion 1c facing the introduction nozzle 16, and the inner end portion of the upper nozzle 15 is accommodated in the tower. The inner end of the upper nozzle 15 exceeds the partition plate 10f and reaches the chamber filled with the neutralizing agent 2. As shown in FIG. 1, the liquid distribution pipe 14 a is a pipe length slightly smaller than the length between both side plates 10 c and is a pipe with a through hole 141 having a length that fits between the inner end of the introduction nozzle 16 and the inner end of the upper nozzle 15. is there. The inlet nozzle 16, the liquid distribution pipe 14a, and the upper nozzle 15 are connected in a straight line by band-fastening both ends of the liquid distribution pipe 14a. The dialysis machine cleaning wastewater 6 led from the upstream portion 91 of the main pipe 9 of the dialysis equipment cleaning drainage 6 through the upstream branch pipe 4 and the introduction nozzle 16 to the liquid distribution pipe 14a is sprinkled from the through hole 141, It falls like a raindrop (Figure 5). Since the depth width W of the tower body 1 is narrow, the dialysis machine washing waste water 6 can be sprayed almost evenly on the upper surface of the packed bed of the neutralizing agent 2 only by passing one liquid distribution pipe 14a. The dialysis machine washing waste water 6 is sprinkled from the liquid distributor 14 so as to wet the neutralizing agent 2, and the neutralizing treatment is performed by dissolving the neutralizing agent 2. The insulator plate 11 is drained, and the dialysis machine washing waste water 6 that sprinkles and flows down is washed away. Since the neutralizing agent 2 is not unnecessarily immersed in the dialysis machine washing waste water 6 for a long time, there is no possibility that the neutralizing agent 2 is thinned or excessively dissolved. The diameters of the introduction nozzle 16, the liquid distribution pipe 14 a, and the upper nozzle 15 are substantially the same as the diameter of the main pipe 9 of the dialysis device washing drainage 6. As the liquid distribution pipe 14a, pipes having the same pipe diameter and pipe length, and different types having different numbers and sizes of through holes 141, pitch arrangement of the through holes 141, and the like are appropriately prepared. If the bands 17a and 17b are removed (a chain line in FIG. 3), the number of the through holes 141 and the size of the through holes 141 can be easily replaced with the liquid distribution pipes 14a. The liquid distribution pipe 14a may be formed by dividing the pipe in half and providing a large number of through holes 141 in the half-divided bowl-shaped portion.

中和剤2は水に溶解して酸性又はアルカリ性を呈する粒状物にして、前記簀子板11上に充填される固形物である。図1のごとく粒状中和剤2が液分散板18近くまで充填される。透析機器洗浄排水6が酸性の場合、中和剤2には水に溶解してアルカリ性を呈する粒状物が用いられる一方、透析機器洗浄排水6がアルカリ性の場合、中和剤2には水に溶解して酸性を呈する粒状物が用いられる。
本実施形態は酢酸などの酸洗浄による殺菌洗浄がなされた透析機器洗浄排水6であり、中和剤2は水に溶解してアルカリを呈する水酸化マグネシウム又は酸化マグネシウム,炭酸カルシウム等の粒状物で、より好ましくは水酸化マグネシウム又は酸化マグネシウムを主成分とする粒状物2aとする。海水法水酸化マグネシウムによって得られる粒径が3mm〜5mmの水酸化マグネシウム粒状物又はそれを所定温度で焼成した酸化マグネシウムを用い、具体的には宇部マテリアルズ株式会社製の水酸化マグネシウム粒状物を用いる。海水法水酸化マグネシウムは、「脱炭酸海水に消石灰乳を添加して生成されるが、その水酸化マグネシウムではコロイド状となり沈降及び洗浄が困難になるので、種晶循環を実施し、粒子を大きくして沈降性,濾過性の良い水酸化マグネシウムが得られる」(『13398の化学商品』,化学工業日報社,165頁,1998)ことから、これを中和処理装置で用いても酸中和処理中にアク等が出ず、またその粒径も適度な大きさで、取扱いに優れたものとなっている。
The neutralizing agent 2 is a solid material that is dissolved in water to form an acidic or alkaline granular material and is filled on the insulator plate 11. As shown in FIG. 1, the granular neutralizer 2 is filled up to the vicinity of the liquid dispersion plate 18. When the dialysis machine washing waste water 6 is acidic, the neutralizing agent 2 is used in the form of a granular material that dissolves in water and exhibits alkalinity. On the other hand, when the dialysis machine washing waste water 6 is alkaline, the neutralizing agent 2 dissolves in water. Thus, granular materials exhibiting acidity are used.
This embodiment is a dialysis machine washing waste water 6 that has been sterilized and washed by acid washing such as acetic acid, and the neutralizing agent 2 is a granular material such as magnesium hydroxide, magnesium oxide, or calcium carbonate that dissolves in water and exhibits an alkali. More preferably, the granular material 2a is composed mainly of magnesium hydroxide or magnesium oxide. Using magnesium hydroxide granules having a particle diameter of 3 mm to 5 mm obtained by seawater method magnesium hydroxide or magnesium oxide fired at a predetermined temperature, specifically, magnesium hydroxide granules made by Ube Materials Co., Ltd. Use. Seawater magnesium hydroxide is produced by adding slaked lime milk to decarbonated seawater, but the magnesium hydroxide becomes colloidal and difficult to settle and wash. Thus, magnesium hydroxide having good sedimentation and filterability can be obtained ”(“ Chemical products of 13398 ”, Chemical Industry Daily, page 165, 1998). During the treatment, no ak or the like is produced, and the particle size is also moderate, which makes it easy to handle.

尚、図3で符号10eは上蓋10e内周に固着する当て部材、符号10eは上蓋10eに係る嵌合部、符号gはパッキンで、これらは補助塔上部1cへの上蓋10eの開け閉めを容易にすると共に簡便且つ確実に蓋ができる構成にある。 3, reference numeral 10 e 1 is a contact member fixed to the inner periphery of the upper lid 10 e, reference numeral 10 e 2 is a fitting portion related to the upper lid 10 e, and reference numeral g is packing, which are used to open and close the upper lid 10 e to the auxiliary tower upper part 1 c. The lid can be easily and reliably covered.

次に、前記構成の中和処理装置を用いた透析機器洗浄排水の一処理方法について説明する。塔本体1の簀子板11上に酸化マグネシウムからなる粒状の中和剤2を所定高さ充填し上蓋10eで蓋をし、開閉弁3を開にしてスタンバイする。人工透析中の排水は本管上流部91から上流側短管92,開閉弁3,下流側短管93,下流部94へと、塔本体1を通らずにそのまま流下する。その後、人工透析が終了し、透析機器が洗浄,消毒される。そして、透析機器類の洗浄で酸性側に傾いた透析機器洗浄排水6が流されると、透析機器洗浄排水6の本管上流部91で透析機器洗浄排水6が酸性側に変わったのを図示しない検出器が検知し、この検出信号が開閉弁3に伝達されて該開閉弁3を閉にする。酸性側に傾いた透析機器洗浄排水6は開閉弁3によって下流側短管93に向かうのが阻止され、上流部91から上流側分岐管4,導入ノズル16を経て液分配管14aに入る。透析機器洗浄排水6は図5のように液分配管14aが緩衝器になってそこに一旦溜められる。液分配管14aが洗浄排水6の流量変動を吸収する。符号62はその溜められた透析機器洗浄排水6の液面を示す。その一方で、液分配管14aに係るパイプの下面側には透孔141が多数形成されていることから、液分配管14aに溜められる透析機器洗浄排水6は同時進行で透孔141から散水61となって垂れ落ちる。中和剤2の充填層に均等に散水できるよう透孔141が所定ピッチで設けられているので、該散水は中和剤2のほぼ全域を濡らすようにして流下し、その過程で中和剤2の溶解により酸性側に傾いていた透析機器洗浄排水6を中和処理していく。中和処理された水7は簀子板11から流れ落ち、液流出管12から下流側分岐管5を通って本管下流部94へと向かう。塔本体1の横断面は洗浄排水6が速やかに流下するに十分な断面積が確保され、且つ簀子板11の下に塔底部1bの空間を設けると共に簀子板11が透析機器洗浄排水6の水を切るので、中和剤2が洗浄排水6に浸されることはない。中和剤2の不必要な消耗がない。
その後、酢酸などによる酸洗浄が終わると、水洗に変わる。すると、透析機器洗浄排水6の本管上流部91でpHが中性に戻ったことを検出器が検知し、その検出信号を受けて開閉弁3が開になって、中性の洗浄排水6は本管上流部91から開閉弁3を通って下流部94に流下する。塔本体1を通過しない。中和処理装置は次なる酸性の透析機器洗浄排水6がくるのを待つこととなる。酸性側に傾いた透析機器洗浄排水6がまた流されると前述と同様の処理をし、透析機器洗浄排水6のpHの円滑な中和処理がなされていく。
Next, a method for treating dialysis machine washing wastewater using the neutralization apparatus having the above-described configuration will be described. The insulator plate 11 of the tower body 1 is filled with granular neutralizing agent 2 made of magnesium oxide to a predetermined height, covered with an upper lid 10e, and the on-off valve 3 is opened to stand by. Drainage during artificial dialysis flows down from the main pipe upstream portion 91 to the upstream short tube 92, the on-off valve 3, the downstream short tube 93, and the downstream portion 94 without passing through the tower body 1. Thereafter, the artificial dialysis is finished, and the dialysis machine is cleaned and disinfected. Then, when the dialysis machine washing wastewater 6 inclined to the acidic side is washed by washing the dialysis equipment, the dialysis equipment washing wastewater 6 is changed to the acidic side in the main pipe upstream portion 91 of the dialysis equipment washing wastewater 6 is not illustrated. This is detected by the detector, and this detection signal is transmitted to the on-off valve 3 to close the on-off valve 3. The dialysis equipment washing waste water 6 inclined to the acidic side is blocked by the on-off valve 3 from going to the downstream short pipe 93 and enters the liquid distribution pipe 14 a from the upstream portion 91 through the upstream branch pipe 4 and the introduction nozzle 16. As shown in FIG. 5, the dialysis machine washing waste water 6 is temporarily stored in the liquid distribution pipe 14a as a buffer. The liquid distribution pipe 14 a absorbs the flow fluctuation of the cleaning waste water 6. Reference numeral 62 indicates the liquid level of the accumulated dialysis machine washing waste water 6. On the other hand, since a large number of through holes 141 are formed on the lower surface side of the pipe related to the liquid distribution pipe 14a, the dialysis device washing waste water 6 stored in the liquid distribution pipe 14a is simultaneously sprinkled from the through holes 141 with water spray 61. It hangs down. Since the through holes 141 are provided at a predetermined pitch so that water can be uniformly sprinkled on the packed bed of the neutralizing agent 2, the water spray flows down so as to wet almost the entire area of the neutralizing agent 2. The dialysis machine washing waste water 6 which has been inclined to the acidic side due to dissolution of 2 is neutralized. The neutralized water 7 flows down from the insulator plate 11 and travels from the liquid outflow pipe 12 through the downstream branch pipe 5 to the main pipe downstream portion 94. The cross section of the tower body 1 has a sufficient cross-sectional area so that the washing waste water 6 can flow down quickly, and a space for the tower bottom 1b is provided below the insulator plate 11, and the insulator plate 11 is the water of the dialysis equipment washing waste water 6. Therefore, the neutralizing agent 2 is not immersed in the cleaning waste water 6. There is no unnecessary consumption of the neutralizing agent 2.
After that, when the acid cleaning with acetic acid or the like is finished, it is changed to washing with water. Then, the detector detects that the pH has returned to neutral in the main pipe upstream portion 91 of the dialysis machine washing drainage 6, and the on-off valve 3 is opened in response to the detection signal, so that the neutral washing drainage 6 Flows down from the main pipe upstream portion 91 through the on-off valve 3 to the downstream portion 94. It does not pass through the tower body 1. The neutralization apparatus waits for the next acidic dialysis machine washing waste water 6 to come. When the dialysis device washing waste water 6 inclined to the acidic side is flowed again, the same treatment as described above is performed, and the pH of the dialysis device washing waste water 6 is smoothly neutralized.

図6は中和処理装置と透析機器洗浄排水本管9の接続を異にした別態様図である。透析機器の洗浄排水用本管9の途中に開閉弁3を設け、該開閉弁3よりも上流側の本管上流部91から上流側分岐管4が下降傾斜して分岐し液分布器14に接続する。また、下流側分岐管5が液流出管12から下降傾斜して雑排水管Mへ接続する。液流出管12,下流側分岐管5には透析機器洗浄排水6を処理した処理水7を流すので、開閉弁3の下流部94に接続しなくても、一般雑排水管Mに接続できる。 FIG. 6 is a diagram showing another embodiment in which the connection between the neutralization treatment device and the dialysis equipment washing / drain main pipe 9 is different. The on-off valve 3 is provided in the middle of the main pipe 9 for washing and draining the dialysis machine, and the upstream branch pipe 4 descends from the main pipe upstream portion 91 upstream of the on-off valve 3 and branches to the liquid distributor 14. Connecting. The downstream-side branch pipe 5 is connected with slopes downward from the liquid outlet pipe 12 to the wastewater pipe M 2. Since the treated water 7 obtained by treating the dialysis device washing waste water 6 flows through the liquid outflow pipe 12 and the downstream branch pipe 5, it can be connected to the general miscellaneous drain pipe M without being connected to the downstream portion 94 of the on-off valve 3.

このように構成した中和処理装置は、塔下部1aに水切り用の簀子板11を設けて該簀子板11上に粒状中和剤2を充填すると共に、塔上部1cに液分配管14aを設置して酸性に傾いた透析機器洗浄排水6をこの液分配管14aに導き、該液分配管14aの透孔141から中和剤2の充填層に散水して流下させ、中和剤2の溶解により中和処理をなすので、透析機器洗浄排水量が多くなり装置が大きくなっても簡単に対応できる。ベッド数規模が大で透析機器の洗浄排水6の処理量が増せば、塔本体1の中和剤2が充填される断面積を大きな塔本体1にし、且つその断面積にほぼ均一に透析機器洗浄排水6が散水できるよう液分配管14aを設けることによって容易に対応できる。透析機器の洗浄排水6の流量に変動があっても、液分配管14aに一旦溜められるので、液分配管14aがバッファーになってその変動を吸収する。さらに透析機器洗浄排水6の流量に変動があっても、塔本体を横断するようにして所定ピッチで設けられた透孔141を通じて充填層上に散水されるので、偏流の虞はない。
そして、塔本体1が充填塔の構造にして、液分配管14aから降り落ちる透析機器洗浄排水6の散水は、粒状中和剤2を濡らしながら流下するので、その過程で中和剤2は中和処理に必要な分だけその散水に溶け込んでいく。簀子板11が塔下部1aの流下する透析機器洗浄排水6の水切り用として働く。液槽等のように液中に中和剤2が長く浸かることがないので、中和剤2が不必要に消耗されない。透析機器洗浄排水6を長期に亘って安定且つ確実に処理できる。
The neutralization treatment apparatus configured in this manner is provided with a draining insulator plate 11 in the tower lower portion 1a and filled with the granular neutralizing agent 2 on the insulator plate 11, and a liquid distribution pipe 14a is installed in the tower upper portion 1c. Then, the dialysis equipment washing waste water 6 inclined to acidity is led to the liquid distribution pipe 14a, and the neutralization agent 2 is dissolved by spraying water from the through hole 141 of the liquid distribution pipe 14a to the packed bed of the neutralizing agent 2. Since the neutralization treatment is performed, the amount of waste water for washing dialysis equipment increases and the apparatus can be easily accommodated. If the number of beds is large and the treatment amount of the washing waste water 6 of the dialysis machine is increased, the cross-sectional area filled with the neutralizing agent 2 of the tower body 1 is changed to the large tower body 1 and the dialysis machine is almost uniformly in the cross-sectional area. This can be easily handled by providing the liquid distribution pipe 14a so that the cleaning waste water 6 can be sprinkled. Even if there is a fluctuation in the flow rate of the washing waste water 6 of the dialysis machine, it is once stored in the liquid distribution pipe 14a, so that the liquid distribution pipe 14a becomes a buffer and absorbs the fluctuation. Furthermore, even if the flow rate of the dialysis machine washing waste water 6 varies, water is sprinkled on the packed bed through the through holes 141 provided at a predetermined pitch so as to cross the tower body, so there is no risk of drift.
And since the tower main body 1 makes the structure of a packed tower and the sprinkling of the dialysis machine washing | cleaning waste_water | drain 6 which falls from the liquid distribution pipe 14a flows down while wetting the granular neutralizing agent 2, the neutralizing agent 2 is in the middle in the process. Dissolve in the sprinkler as much as necessary for the sum treatment. The insulator plate 11 serves to drain the dialysis equipment washing drainage 6 flowing down the tower lower part 1a. Since the neutralizing agent 2 is not soaked in the liquid for a long time as in a liquid tank or the like, the neutralizing agent 2 is not consumed unnecessarily. The dialysis machine washing waste water 6 can be treated stably and reliably over a long period of time.

上流側分岐管4が開閉弁3よりも上流側の本管上流部91から水平又は下降傾斜して分岐し液分布器14に接続し、また下流側分岐管5が液流出管12から水平又は下降傾斜して開閉弁3よりも下流側の本管下流部94へと接続するか、又は液流出管12から水平又は下降傾斜して雑排水管Mへ接続するので、重力落差を利用して透析機器洗浄排水6を難なく処理できる。透析機器洗浄排水6の処理に何ら動力を要しない。   The upstream branch pipe 4 branches from the main pipe upstream portion 91 upstream of the on-off valve 3 in a horizontal or descending manner and branches to connect to the liquid distributor 14, and the downstream branch pipe 5 extends horizontally from the liquid outlet pipe 12. Since it is inclined downward and connected to the main pipe downstream portion 94 downstream of the on-off valve 3, or is connected to the miscellaneous drainage pipe M while being inclined horizontally or downward from the liquid outflow pipe 12, the gravity drop is utilized. The dialysis machine washing waste water 6 can be treated without difficulty. No power is required for the treatment of the dialysis machine washing waste water 6.

また中和剤2に水酸化マグネシウム又は酸化マグネシウムを主成分とする粒状物を用いているので、中和剤2を濡らすように液分布器14から透析機器洗浄排水6を散水して流下させることによって、中和剤2が適度に溶解し上手く中和処理ができる。水酸化マグネシウム又は酸化マグネシウムを主成分とする粒状物2aを用いているので、天然岩石粒子等に比べ中和反応が速く、充填塔の充填物のごとく濡らすだけで十分となる。塔本体1内に充填する量も少なくて済む。海水法水酸化マグネシウムからなる中和剤2を用いると、粒子を大きくして沈降性,濾過性の良いものが得られることから、酸中和処理中にアクが出ず、且つ粒径も適度な大きさで、作業性,取扱いに一段と優れたものとなる。
さらに、塔本体1をその正面板10aの縦横長さに比べ奥行き幅Wが狭い略方形体に形成し、且つ該塔本体1の奥行き幅Wの略中間地点を一直線状に1本の前記液分配管14aが横断するよう配設しているので、塔本体1及び液分配管14aを簡単な構造にして、加えて中和剤2の充填層に透析機器洗浄排水6を均等散水し易くなる。奥行き幅Wが狭いので場所をとらず、少ない空きスペースでも図2のごとく建物壁に寄り添わせて本中和処理装置を設置できる。
In addition, since the neutralizing agent 2 is made of granular material mainly composed of magnesium hydroxide or magnesium oxide, the dialysis device washing waste water 6 is sprinkled down from the liquid distributor 14 so as to wet the neutralizing agent 2. Thus, the neutralizing agent 2 is appropriately dissolved and can be neutralized well. Since the granular material 2a containing magnesium hydroxide or magnesium oxide as a main component is used, the neutralization reaction is faster than that of natural rock particles and the like, and it is sufficient to wet it like a packed column. The amount to be filled in the tower body 1 can be small. When neutralizing agent 2 made of seawater magnesium hydroxide is used, particles can be enlarged to obtain a product with good sedimentation and filterability. With its large size, it is much more excellent in workability and handling.
Furthermore, the tower main body 1 is formed into a substantially rectangular shape having a depth width W narrower than the length and breadth of the front plate 10a, and the intermediate point of the depth width W of the tower main body 1 is aligned in a straight line. Since the distribution pipe 14a is arranged so as to cross, the tower main body 1 and the liquid distribution pipe 14a have a simple structure, and in addition, the dialysis equipment washing waste water 6 can be easily sprinkled into the packed bed of the neutralizing agent 2. . Since the depth width W is narrow, the present neutralization apparatus can be installed in close proximity to the building wall as shown in FIG.

尚、本発明においては、前記実施形態,実施例に示すものに限られず、目的,用途に応じて本発明の範囲で種々変更できる。塔本体1,中和剤2,上流側分岐管4,下流側分岐管5,透析機器洗浄排水6の本管9,雑配水管M等の形状,大きさ,材質,成分組成等は用途に合わせて本発明の範囲内で適宜選択できる。   The present invention is not limited to those shown in the above-described embodiments and examples, and various modifications can be made within the scope of the present invention depending on the purpose and application. The shape, size, material, composition, etc. of the tower body 1, neutralizer 2, upstream branch pipe 4, downstream branch pipe 5, main pipe 9 of dialysis equipment washing drainage 6, miscellaneous water pipe M, etc. In addition, they can be appropriately selected within the scope of the present invention.

本発明の透析機器洗浄排水の中和処理装置の一形態で、透析機器の洗浄排水用本管に接続してなる中和処理装置の概略正面断面図である。1 is a schematic front cross-sectional view of a neutralization apparatus connected to a main pipe for washing and draining dialysis equipment in one embodiment of the dialysis equipment washing and drainage neutralization apparatus of the present invention. 図1の側面図である。It is a side view of FIG. (イ)が図1のI-I線矢視図で、(ロ)が液分布器の横断面図で、(ハ)が塔本体の上蓋周りの拡大図である。(A) is a cross-sectional view taken along the line II of FIG. 1, (b) is a cross-sectional view of the liquid distributor, and (c) is an enlarged view around the top cover of the tower body. 蓋を外した状態の中和処理装置の平面図である。It is a top view of the neutralization processing apparatus of the state which removed the cover. 液分布器周りの拡大図である。It is an enlarged view around a liquid distributor. 別態様の透析機器洗浄排水本管,雑排水管との接続例を示す中和処理装置の説明図である。It is explanatory drawing of the neutralization processing apparatus which shows the example of a connection with the dialysis equipment washing | cleaning drainage main pipe and miscellaneous drainage pipe of another aspect.

符号の説明Explanation of symbols

1 塔本体
1a 塔下部
1b 塔底部
1c 塔上部
10a 正面板
11 簀子板
12 液流出器
14 液分布器
14a 液分配器
141 透孔
2 中和剤
2a 水酸化マグネシウム又は酸化マグネシウムを主成分とする粒状物
3 開閉弁
4 上流側分岐管
6 透析機器洗浄排水(洗浄排水)
5 下流側分岐管
9 透析機器洗浄排水の本管
W 奥行き幅
DESCRIPTION OF SYMBOLS 1 Tower main body 1a Tower lower part 1b Tower bottom part 1c Tower upper part 10a Front board 11 Insulator board 12 Liquid outflow device 14 Liquid distributor 14a Liquid distributor 141 Through-hole 2 Neutralizing agent 2a Granular substance which has magnesium hydroxide or magnesium oxide as a main component 3 Open / close valve 4 Branch pipe upstream 6 Washing drainage for dialysis equipment (washing drainage)
5 Downstream branch pipe 9 Main pipe for washing and draining dialysis equipment W Depth width

Claims (4)

塔内の下部に水切り用簀子板を設け、該簀子板の下方の塔底部に液流出管を設けると共に、塔上部に透析機器の洗浄排水を散水する液分布器を設けた塔本体(1)と、
水に溶解して酸性又はアルカリ性を呈する粒状物にして、前記簀子板上に充填される固形の中和剤(2)と、を具備し、該中和剤を濡らすように前記液分布器から透析機器の洗浄排水を散水して流下させ、該中和剤の溶解により中和処理をなすことを特徴とする透析機器洗浄排水の中和処理装置。
A tower main body (1) provided with a draining insulator plate at the lower part of the tower, a liquid outflow pipe at the bottom of the tower below the insulator board, and a liquid distributor for sprinkling washing waste water from the dialysis equipment at the upper part of the tower When,
A solid neutralizing agent (2) which is dissolved in water and exhibits acidity or alkalinity, and is filled on the insulator plate, from the liquid distributor so as to wet the neutralizing agent. A neutralization treatment apparatus for dialysis equipment washing waste water, wherein the washing waste water from the dialysis equipment is sprinkled down and neutralized by dissolving the neutralizing agent.
塔内の下部に水切り用簀子板を設け、該簀子板の下方の塔底部に液流出管を設けると共に、塔上部に透析機器の洗浄排水を散水する液分布器を設けた塔本体(1)と、
水に溶解してアルカリ性を呈する粒状物にして、前記簀子板上に充填される固形の中和剤(2)と、
透析機器の洗浄排水用本管の途中に設けられる開閉弁(3)と、
該開閉弁よりも上流側の前記本管から略水平又は下降傾斜して分岐し前記液分布器へ導く上流側分岐管(4)と、
前記液流出管から水平又は下降傾斜して前記開閉弁よりも下流側の前記本管へと接続する下流側分岐管(5)、又は前記液流出管から略水平又は下降傾斜して雑排水管へと接続する下流側分岐管(5)と、を具備し、前記中和剤を濡らすように前記液分布器から透析機器の洗浄排水を散水して流下させ、該中和剤の溶解により中和処理をなすことを特徴とする透析機器洗浄排水の中和処理装置。
A tower main body (1) provided with a draining insulator plate at the lower part of the tower, a liquid outflow pipe at the bottom of the tower below the insulator board, and a liquid distributor for sprinkling washing waste water from the dialysis equipment at the upper part of the tower When,
A solid neutralizing agent (2) which is dissolved in water to form an alkaline substance and filled on the insulator plate;
An on-off valve (3) provided in the middle of the main pipe for washing and draining dialysis equipment,
An upstream branch pipe (4) branched from the main pipe upstream of the on-off valve substantially horizontally or downwardly inclined and led to the liquid distributor;
A downstream branch pipe (5) connected to the main pipe downstream from the on-off valve with a horizontal or downward inclination from the liquid outflow pipe, or a miscellaneous drain pipe with a substantially horizontal or downward inclination from the liquid outflow pipe. A downstream branch pipe (5) connected to the basin, and the washing effluent of the dialysis machine is sprinkled down from the liquid distributor so as to wet the neutralizer, and the neutralizer is dissolved by A neutralization treatment device for washing waste water from dialysis equipment, characterized by performing sum treatment.
前記中和剤が水酸化マグネシウム又は酸化マグネシウムを主成分とする粒状物からなり、且つ前記液分布器がパイプの下面側に透孔を多数形成した液分配管からなる請求項2記載の透析機器洗浄排水の中和処理装置。 The dialysis machine according to claim 2, wherein the neutralizing agent is made of a granular material mainly composed of magnesium hydroxide or magnesium oxide, and the liquid distributor is made of a liquid pipe having a large number of through holes formed on the lower surface side of the pipe. Cleaning wastewater neutralization treatment equipment. 前記塔本体の外形をその正面板の縦横長さに比べ奥行き幅が狭い略方形体に形成し、且つ該塔本体の外形の奥行き幅の略中間地点を一直線状に1本の前記液分配管が横断するよう配設されてなる請求項3記載の透析機器洗浄排水の中和処理装置。 The outer shape of the tower main body is formed in a substantially rectangular shape having a depth width smaller than the length and width of the front plate, and the liquid pipe is arranged in a straight line at a substantially middle point of the depth width of the outer shape of the tower main body. The neutralization processing apparatus of the dialysis equipment washing waste_water | drain of Claim 3 arrange | positioned so that may cross | intersect.
JP2004382009A 2004-12-28 2004-12-28 Dialysis equipment washing wastewater neutralization treatment equipment Expired - Fee Related JP4643254B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004382009A JP4643254B2 (en) 2004-12-28 2004-12-28 Dialysis equipment washing wastewater neutralization treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004382009A JP4643254B2 (en) 2004-12-28 2004-12-28 Dialysis equipment washing wastewater neutralization treatment equipment

Publications (2)

Publication Number Publication Date
JP2006187683A true JP2006187683A (en) 2006-07-20
JP4643254B2 JP4643254B2 (en) 2011-03-02

Family

ID=36795343

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004382009A Expired - Fee Related JP4643254B2 (en) 2004-12-28 2004-12-28 Dialysis equipment washing wastewater neutralization treatment equipment

Country Status (1)

Country Link
JP (1) JP4643254B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111320307A (en) * 2020-03-20 2020-06-23 新昌县梅维斯环保有限公司 Chemical production wastewater purification and discharge device in convection type and atomization neutralization
WO2023009389A3 (en) * 2021-07-26 2023-03-09 Fresenius Medical Care Holdings, Inc. Medical fluid drain containers and related systems and methods

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108314207B (en) * 2018-02-01 2019-09-24 海宁华翔漂染科技有限公司 A kind for the treatment of method of printing and dying wastewater

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS562886A (en) * 1979-06-19 1981-01-13 Ebara Infilco Co Ltd Neutralization of acidic water containing iron ion
JPH11299883A (en) * 1998-04-24 1999-11-02 Akihisa Minato Waste water treatment unit for dialysis apparatus
JP2001269670A (en) * 2000-03-24 2001-10-02 Nikkiso Co Ltd Neutralizing treatment device for waste liquid generated from artificial dialysis
JP2001321782A (en) * 2000-05-12 2001-11-20 Tabai Espec Corp Apparatus for treating acid washing wastewater of artificial dialyser
JP2002282869A (en) * 2001-03-23 2002-10-02 Setsuo Kobayashi pH ADJUSTING DEVICE FOR WASTEWATER FROM ARTIFICIAL DIALYSIS
JP2004130293A (en) * 2002-10-14 2004-04-30 Setsuo Kobayashi pH ADJUSTER

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS562886A (en) * 1979-06-19 1981-01-13 Ebara Infilco Co Ltd Neutralization of acidic water containing iron ion
JPH11299883A (en) * 1998-04-24 1999-11-02 Akihisa Minato Waste water treatment unit for dialysis apparatus
JP2001269670A (en) * 2000-03-24 2001-10-02 Nikkiso Co Ltd Neutralizing treatment device for waste liquid generated from artificial dialysis
JP2001321782A (en) * 2000-05-12 2001-11-20 Tabai Espec Corp Apparatus for treating acid washing wastewater of artificial dialyser
JP2002282869A (en) * 2001-03-23 2002-10-02 Setsuo Kobayashi pH ADJUSTING DEVICE FOR WASTEWATER FROM ARTIFICIAL DIALYSIS
JP2004130293A (en) * 2002-10-14 2004-04-30 Setsuo Kobayashi pH ADJUSTER

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111320307A (en) * 2020-03-20 2020-06-23 新昌县梅维斯环保有限公司 Chemical production wastewater purification and discharge device in convection type and atomization neutralization
CN111320307B (en) * 2020-03-20 2021-08-27 上海同金化工有限公司 Chemical production wastewater purification and discharge device in convection type and atomization neutralization
WO2023009389A3 (en) * 2021-07-26 2023-03-09 Fresenius Medical Care Holdings, Inc. Medical fluid drain containers and related systems and methods
US12042587B2 (en) 2021-07-26 2024-07-23 Fresenius Medical Care Holdings, Inc. Medical fluid drain containers and related systems and methods

Also Published As

Publication number Publication date
JP4643254B2 (en) 2011-03-02

Similar Documents

Publication Publication Date Title
US8834716B2 (en) Water treatment device
JP2007130585A (en) Activated carbon adsorption system
JP4643254B2 (en) Dialysis equipment washing wastewater neutralization treatment equipment
JP2011117184A (en) System for reusing domestic water
JP2009161601A (en) Organism desulfurization apparatus
JP4035201B2 (en) Rainwater and middle water circulation equipment
JP2005219041A (en) Neutralizing apparatus for waste water from cleaning and sterilizing process of dialyzing apparatus
US20040140250A1 (en) SSF/x slow sand filter
JP2007075763A (en) Device for neutralizing waste water of personal dialyzer
US3881700A (en) Water treatment plant
JP6249086B1 (en) Cleaning device and cleaning method for chemical injection nozzle
CN205974091U (en) Integration acid waste water automatic treating device
CN209456187U (en) Sewage treatment equipment is used in titanium white production processing
RU2785322C1 (en) Apparatus for reagent distribution in the fluidised bed
CN108218019A (en) A kind of sewage treatment unit
US1720185A (en) Liquid-clarifying apparatus
CN206232480U (en) The processing unit of hydrolysis acidification pool sediment and scum silica frost
CN211871657U (en) Accurate control type sewage multistep treatment device
JP2000050797A (en) Apparatus for washing fresh tea leaf
JP2004230349A (en) Waste water treatment apparatus
RU2006105662A (en) SEWAGE TREATMENT DEVICE
CN205699779U (en) A kind of industrial purifier of recycling water resource
JPH0144165Y2 (en)
WO1992002286A1 (en) Method of treating liquids and apparatus therefor
JP5704867B2 (en) Aeration equipment for water treatment, water treatment equipment

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20071225

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20101029

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20101104

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: 20101124

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: 20101202

R150 Certificate of patent or registration of utility model

Ref document number: 4643254

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

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

Free format text: PAYMENT UNTIL: 20131210

Year of fee payment: 3

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

Free format text: PAYMENT UNTIL: 20131210

Year of fee payment: 3

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

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

Free format text: PAYMENT UNTIL: 20131210

Year of fee payment: 3

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees