JPS623148Y2 - - Google Patents
Info
- Publication number
- JPS623148Y2 JPS623148Y2 JP4485081U JP4485081U JPS623148Y2 JP S623148 Y2 JPS623148 Y2 JP S623148Y2 JP 4485081 U JP4485081 U JP 4485081U JP 4485081 U JP4485081 U JP 4485081U JP S623148 Y2 JPS623148 Y2 JP S623148Y2
- Authority
- JP
- Japan
- Prior art keywords
- filth
- suction
- water
- suction pump
- suction device
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 31
- 244000005700 microbiome Species 0.000 claims description 7
- 238000007789 sealing Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 230000001902 propagating effect Effects 0.000 claims description 2
- 239000002699 waste material Substances 0.000 claims description 2
- 239000003206 sterilizing agent Substances 0.000 claims 1
- 239000000126 substance Substances 0.000 description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 7
- 239000007787 solid Substances 0.000 description 6
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000000645 desinfectant Substances 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000295146 Gallionellaceae Species 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
Landscapes
- Accommodation For Nursing Or Treatment Tables (AREA)
Description
【考案の詳細な説明】
本考案は病院等にあつて、患者の汚物を器体内
に吸引収受した後、当該収受汚物を便所等に捨て
るため用いられている汚物吸引器用として、これ
に連結して用いられる排気装置の改良に関するも
のである。[Detailed description of the invention] The present invention is designed to be connected to a filth suction device that is used in hospitals, etc., to suck up patient filth into a container and then dispose of the collected filth in a toilet, etc. This invention relates to improvements to exhaust systems used in
既知の通り、この種汚物吸引器4は第1図に示
す通り汚物吸引口1が開口されている汚物吸引パ
イプ2を、器体3に連結し、これまた当該器体3
に連結されている排気口5を、別体である排気装
置6に適時連結して使用するものであここで当該
従来の同排気装置6はバツフアタンク7と吸引ポ
ンプ8とからなり、この吸引ポンプ8内には封水
Aを給水口9から供与しておき、同ポンプ8を運
転稼動することにより、上記吸引器4の器体3内
を負圧となし、当該負圧を利用して前記の汚物吸
引口1から汚物吸引パイプ2を介して器体3内に
汚物を吸引収受するようにしている。 As is known, this type of filth suction device 4 connects a filth suction pipe 2 with a filth suction port 1 opened to a container body 3, as shown in FIG.
The exhaust port 5, which is connected to the 8 is supplied with sealed water A from the water supply port 9, and by operating the same pump 8, a negative pressure is created in the container body 3 of the suction device 4, and the negative pressure is used to The filth is sucked and received into the container body 3 from the filth suction port 1 through the filth suction pipe 2.
そして、この場合吸引された汚物を消毒するた
め、予め器体3内には、フエノール系、またはア
ルコール系の薬液Bを投入しておき、上記の汚物
吸引操作が終れば器体3の蓋10を外し、器体3
内の収受汚物を適所に捨てることになるが、図中
11が吸引ポンプ8の排気口を、12は封水の排
水口を示している。 In this case, in order to disinfect the suctioned filth, a phenol-based or alcohol-based chemical solution B is put into the container 3 in advance, and after the above-mentioned filth suction operation is completed, the lid 10 of the container 3 is closed. Remove the body 3
In the figure, 11 indicates the exhaust port of the suction pump 8, and 12 indicates the water sealing drain port.
さてこのような汚物吸引器4を排気装置6によ
り稼動した場合、もちろん或期間は正常な吸引機
能を発揮するのであるが、使用を続けていくと吸
引機能が低下してしまい、遂には吸引ポンプ8の
回転自体が停止してしまう事態が生じている。 Now, when such a filth suction device 4 is operated by the exhaust device 6, it will of course exhibit normal suction function for a certain period of time, but as it continues to be used, the suction function will deteriorate and eventually the suction pump will fail. A situation has arisen in which the rotation of 8 itself stops.
そこで従来このような状態となつたとき、採ら
れている対策手段は、吸引ポンプ8の封水Aを、
排水口12から排出させるだけでなく、当該ポン
プ8内の各所からも検出される固形物を除去する
ことであり、このような作業の後、運転を再開し
なければならないため、当該作業に可成りの時間
と労力を費さねばならないだけでなく、その間汚
物吸引器4は使用不能となるため、予備の汚物吸
引器用排気装置を別途備えておかねばならないと
いつた問題があつた。 Conventionally, when such a situation occurs, the countermeasure taken is to seal water A of the suction pump 8,
The objective is not only to discharge the solids from the drain port 12, but also to remove the solids detected from various parts of the pump 8. After such work, operation must be restarted, so it is necessary to Not only does this require a considerable amount of time and effort, but the filth suction device 4 becomes unusable during this time, so there is a problem in that a spare exhaust device for the filth suction device must be provided separately.
本考案はこのような支障を解消して、長期にわ
たる汚物吸引器の正常運転が保証できる排気装置
を提供しようとするもので、これを図面によつて
詳記すれば、第1乃至第4図に示す通り何れの実
施例にあつても、前記した吸引ポンプ8内に供与
した封水Aを、所定の温度条件に加熱または冷却
するための、熱交換手段13が具備されており、
しかも当該温度条件とは上記封水A中における好
気性微生物の繁殖を阻止するものでなくてはなら
ない。 The present invention aims to eliminate such problems and provide an exhaust system that can guarantee the normal operation of the filth suction device over a long period of time. As shown in the figure, in any of the embodiments, a heat exchange means 13 is provided for heating or cooling the sealed water A supplied into the suction pump 8 to a predetermined temperature condition.
Moreover, the temperature conditions must be such as to prevent the growth of aerobic microorganisms in the sealed water A.
こゝで前記第1図に既述した装置例にあつて
は、上記熱交換手段13として、吸引ポンプ8内
に電熱ヒータ14を、封水Aと当接するように内
装したものが示されておるのに対し、第2図の場
合には吸引ポンプ8に高周波加熱器15を臨設し
て、熱交換手段13としている。 In the example of the apparatus already described in FIG. 1, an electric heater 14 is installed inside the suction pump 8 as the heat exchange means 13 so as to come into contact with the seal water A. On the other hand, in the case of FIG. 2, a high frequency heater 15 is provided on the suction pump 8 to serve as a heat exchange means 13.
さらに第3、第4図の熱交換手段13は、給水
源16から給水口9を経て封水Aを供与する給水
ライン17と、排水口12に連結した排水ライン
18とにより循環ライン19を形成すると共に、
当該ライン19には循環ポンプ20を直列に連結
すると共に、この循環ライン19の適所には第3
図のようにヒータ21か、第4図の如く冷却器2
2を付設し、これによつて封水Aを循環ポンプ2
0の稼動により、当該ライン19に回流させ、こ
の回流する封水を、ヒータ21で加温するか冷却
器22により冷却するよう構成してある。 Further, the heat exchange means 13 in Figs. 3 and 4 includes a water supply line 17 for supplying the sealing water A from a water supply source 16 through the water supply port 9, and a drainage line 18 connected to the drainage port 12 to form a circulation line 19.
A circulation pump 20 is connected in series to the line 19, and a third pump is connected in an appropriate position to the circulation line 19.
As shown in the figure, a heater 21 or a cooler 2 as shown in FIG.
2 is attached, so that the seal water A is circulated by pump 2
0 is operated to circulate the sealing water through the line 19, and the circulating sealing water is heated by a heater 21 or cooled by a cooler 22.
こゝで上記加温の場合は45℃以上の温度条件が
封水に与えられることが望ましく、また冷却手段
をとるときは5℃以下とするのが最適である。 In the case of the above-mentioned heating, it is desirable that the sealed water be given a temperature condition of 45°C or higher, and when cooling means is used, it is optimal to set the temperature to 5°C or lower.
本考案上記各種実施例によつて具現される通
り、従来の排気装置における吸引ポンプ8内の封
水Aを、当該封水中に好気性微生物が繁殖するこ
とを阻止する温度条件に、加熱または冷却する熱
交換手段13を具備させるよう構成した結果、こ
のような熱交換手段13をもたない従来装置にあ
つては、封水の交換や吸引ポンプの洗滌作業を不
可欠とし、特にアルコール系の殺菌消毒剤を吸引
器内に投入使用した場合には約7日間程度で封水
を交換しなければならなかつたのに対し、全く吸
引ポンプ8の回転状態に異常が生ずることなく、
汚物吸引器の吸引能力が低下することなしに、そ
の稼動を支障なく持続することができた。 As embodied in the various embodiments of the present invention, the sealed water A in the suction pump 8 in a conventional exhaust system is heated or cooled to a temperature condition that prevents aerobic microorganisms from propagating in the sealed water. As a result of the structure having the heat exchange means 13, which does not have such a heat exchange means 13, it is necessary to replace seal water and clean the suction pump, especially when using alcohol-based sterilizers. When a disinfectant was put into the suction device, the water seal had to be replaced after about 7 days, but no abnormality occurred in the rotational state of the suction pump 8.
The suction capacity of the filth suction device was not reduced, and the operation of the filth suction device could be continued without any problems.
このような結果が得られたのは、前記のように
吸引ポンプの回転を阻害し吸引力を低下させる固
形物が、一般に予想される配管系統からの鉄錆、
鉄バクテリア等に依存するものでなく、また汚物
吸引器4に吸引れた汚物が吸引ポンプ8中に流入
するものでもなく、さらにまた上記の如く投入さ
れたフエノール系、アルコール系薬液が変化を受
けて固形物に生成されたものでもなく、封水中に
極めて豊富な溶存酸素が存すると共に、当該酸素
(空気)が次々と補給される条件が満足されてお
り、しかもかゝる吸引装置にあつては、上記のよ
うにフエノール系、アルコール系の薬液が使用さ
れ、さらにまた汚物吸引器4は病室、手術室等の
温度条件下にて使用されることから、溶存酸素の
存する状態で発生するバクテリア等の原生動物す
なわち好気性微生物のスライム(群落)が当該固
形物の本質となつていることに起因するのであ
る。 This result was obtained because the solid matter that obstructs the rotation of the suction pump and reduces the suction power as described above is generally expected to be due to iron rust from the piping system,
It does not depend on iron bacteria, etc., nor does the filth sucked into the filth suction device 4 flow into the suction pump 8, and furthermore, the phenol-based and alcohol-based chemicals introduced as described above undergo no change. It is not generated in solid matter, and there is an extremely rich amount of dissolved oxygen in the sealed water, and the conditions for continuous replenishment of oxygen (air) are satisfied, and the suction device is As mentioned above, phenol-based and alcohol-based chemicals are used, and the filth suction device 4 is used under temperature conditions such as hospital rooms and operating rooms, so bacteria generated in the presence of dissolved oxygen is prevented. This is due to the fact that the essence of the solid material is slime (community) of protozoa such as aerobic microorganisms.
そして固形物の本質が上記の如く好気性微生物
のスライムであることも確認し得たが、当該微生
物は上記の通り酸素の存在と、温度条件に加え
て、汚物吸引器4に投入されたアルコール系等の
薬液が蒸気となつて汚物吸引器用排気装置6に吸
引されて行き、上記封水Aに溶解されることか
ら、特にフエノール系よりも原生動物の栄養源
(餌)として優位なアルコール系薬液の場合、固
形物による支障が増大することになるのであり、
本考案にあつては所要温度条件を封水Aに与える
熱交換手段13が、上記好気性微生物の繁殖を阻
止することになり、これにより固形物が発生せ
ず、従来装置における前記各種の難点を実質的に
解消でき、信頼性の高いものを提供できることに
なる。 It was also confirmed that the essence of the solid material was the slime of aerobic microorganisms as described above, but the microorganisms were formed by the presence of oxygen and temperature conditions as described above, as well as by the presence of alcohol injected into the waste suction device 4. Alcohol-based chemicals are particularly superior to phenol-based drugs as a nutrient source (feed) for protozoa, as chemical solutions such as alcohol-based chemicals turn into vapor and are sucked into the filth suction device exhaust device 6 and are dissolved in the sealed water A. In the case of chemical solutions, the hindrance caused by solids increases,
In the present invention, the heat exchange means 13 that provides the required temperature conditions to the sealed water A prevents the growth of the aerobic microorganisms, thereby preventing the generation of solid matter and eliminating the various drawbacks of the conventional devices. This means that the problem can be virtually eliminated, and a highly reliable product can be provided.
第1図は本考案に係る吸引器用排気装置の一実
施例を示す配管説明図、第2、第3図は同装置の
他実施例による配管説明図で第4図は第3図のも
のと異種の熱交換手段を示した同装置の部分配管
説明図である。
1……汚物吸引口、2……汚物吸引パイプ、4
……汚物吸引器、7……バツフアタンク、8……
吸引ポンプ、13……熱交換手段、14……電熱
ヒータ、15……高周波加熱コイル、17……給
水ライン、18……排水ライン、19……循環ラ
イン、20……循環ポンプ、21……ヒータ、2
2……冷却器、A……封水、B……薬液(殺菌消
毒剤)。
Fig. 1 is an explanatory diagram of piping showing one embodiment of the suction exhaust device according to the present invention, Figs. 2 and 3 are explanatory diagrams of piping according to other embodiments of the same device, and Fig. 4 is the same as that of Fig. 3. FIG. 2 is a partial piping explanatory diagram of the same device showing different types of heat exchange means. 1...Fility suction port, 2...Fility suction pipe, 4
...Fility suction device, 7...Batua tank, 8...
Suction pump, 13... Heat exchange means, 14... Electric heater, 15... High frequency heating coil, 17... Water supply line, 18... Drainage line, 19... Circulation line, 20... Circulation pump, 21... Heater, 2
2... Cooler, A... Water seal, B... Chemical solution (sterilizing disinfectant).
Claims (1)
ンクに、吸引ポンプが連結され、この吸引ポン
プの稼動により、殺菌消毒剤が投入されている
当該汚物吸引器の器体内を吸引排気して、同器
体内を負圧とすることにより、当該器体内に、
上記汚物吸引器の汚物吸引口から汚物吸引パイ
プを介して、病人等の汚物を吸入収受させ得る
ようにし、かつ、上記吸引ポンプが、給水自在
な給水口と、封水の排水口とを具有しているも
のにおいて、上記吸引ポンプ内の封水を、当該
封水中に好気性微生物が繁殖することを阻止す
る温度条件に、加熱または冷却する熱交換手段
を具備してなる汚物吸引器用排気装置。 (2) 熱交換手段が、吸引ポンプ内に設けた電熱ヒ
ータを、封水と当接するよう配装して構成され
ている実用新案登録請求の範囲第1項記載の汚
物吸引器用排気装置。 (3) 熱交換手段が、吸引ポンプに臨設した高周波
加熱器により構成されている実用新案登録請求
の範囲第1項記載の汚物吸引器用排気装置。 (4) 熱交換手段が、吸引ポンプの給水ライン、排
水ラインおよび循環ポンプによる直列連結の循
環ラインと、当該循環ラインに付設したヒータ
または冷却器とにより構成されている実用新案
登録請求の範囲第1項記載の汚物吸引器用排気
装置。[Scope of Claim for Utility Model Registration] (1) A suction pump is connected to a buffer tank that connects the exhaust port side of the filth suction device, and a sterilizing agent is introduced into the filth suction device by the operation of this suction pump. By suctioning and exhausting the inside of the container to create a negative pressure inside the container,
The filth suction port of the filth suction device is configured to inhale and collect the filth of a sick person, etc. through the filth suction pipe, and the suction pump includes a water supply port through which water can be freely supplied and a water sealing drain port. an exhaust system for a waste suction device, comprising a heat exchange means for heating or cooling the sealed water in the suction pump to a temperature condition that prevents aerobic microorganisms from propagating in the sealed water. . (2) The exhaust device for a filth suction device according to claim 1, wherein the heat exchange means is constructed by disposing an electric heater provided in the suction pump so as to come into contact with the sealed water. (3) The exhaust device for a filth suction device according to claim 1, wherein the heat exchange means is constituted by a high-frequency heater installed next to the suction pump. (4) Utility model registration claim No. 1 in which the heat exchange means is composed of a circulation line connected in series with a water supply line of a suction pump, a drainage line, and a circulation pump, and a heater or cooler attached to the circulation line. The exhaust device for a filth suction device according to item 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4485081U JPS623148Y2 (en) | 1981-03-30 | 1981-03-30 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4485081U JPS623148Y2 (en) | 1981-03-30 | 1981-03-30 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57157331U JPS57157331U (en) | 1982-10-02 |
| JPS623148Y2 true JPS623148Y2 (en) | 1987-01-24 |
Family
ID=29841771
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4485081U Expired JPS623148Y2 (en) | 1981-03-30 | 1981-03-30 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS623148Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0724676B2 (en) * | 1990-03-29 | 1995-03-22 | 三洋電機株式会社 | Sewage discharge treatment equipment |
-
1981
- 1981-03-30 JP JP4485081U patent/JPS623148Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57157331U (en) | 1982-10-02 |
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