JPH02203992A - Device for washing and purifying article - Google Patents
Device for washing and purifying articleInfo
- Publication number
- JPH02203992A JPH02203992A JP1023793A JP2379389A JPH02203992A JP H02203992 A JPH02203992 A JP H02203992A JP 1023793 A JP1023793 A JP 1023793A JP 2379389 A JP2379389 A JP 2379389A JP H02203992 A JPH02203992 A JP H02203992A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- water
- sterile water
- sent
- article
- 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.)
- Pending
Links
- 238000005406 washing Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 129
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 96
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000008223 sterile water Substances 0.000 claims description 36
- 238000004519 manufacturing process Methods 0.000 claims description 25
- 238000004140 cleaning Methods 0.000 claims description 19
- 238000001914 filtration Methods 0.000 claims description 12
- 239000004576 sand Substances 0.000 claims description 3
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims 1
- 239000007789 gas Substances 0.000 abstract description 10
- 238000000746 purification Methods 0.000 abstract description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 6
- 238000004090 dissolution Methods 0.000 abstract description 6
- 239000001301 oxygen Substances 0.000 abstract description 6
- 229910052760 oxygen Inorganic materials 0.000 abstract description 6
- 239000012530 fluid Substances 0.000 abstract description 5
- 230000005855 radiation Effects 0.000 abstract 3
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 239000000047 product Substances 0.000 description 12
- 239000000126 substance Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 5
- 239000012535 impurity Substances 0.000 description 5
- 102000004169 proteins and genes Human genes 0.000 description 5
- 108090000623 proteins and genes Proteins 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000007791 liquid phase Substances 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 238000009287 sand filtration Methods 0.000 description 4
- 239000003925 fat Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- LFYXNXGVLGKVCJ-FBIMIBRVSA-N 2-methylisoborneol Chemical compound C1C[C@@]2(C)[C@](C)(O)C[C@@H]1C2(C)C LFYXNXGVLGKVCJ-FBIMIBRVSA-N 0.000 description 2
- LFYXNXGVLGKVCJ-UHFFFAOYSA-N 2-methylisoborneol Natural products C1CC2(C)C(C)(O)CC1C2(C)C LFYXNXGVLGKVCJ-UHFFFAOYSA-N 0.000 description 2
- GZSOSUNBTXMUFQ-NJGQXECBSA-N 5,7,3'-Trihydroxy-4'-methoxyflavone 7-O-rutinoside Natural products O(C[C@@H]1[C@@H](O)[C@H](O)[C@@H](O)[C@H](Oc2cc(O)c3C(=O)C=C(c4cc(O)c(OC)cc4)Oc3c2)O1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@H](C)O1 GZSOSUNBTXMUFQ-NJGQXECBSA-N 0.000 description 2
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 2
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- 239000003599 detergent Substances 0.000 description 2
- GZSOSUNBTXMUFQ-YFAPSIMESA-N diosmin Chemical compound C1=C(O)C(OC)=CC=C1C(OC1=C2)=CC(=O)C1=C(O)C=C2O[C@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO[C@H]2[C@@H]([C@H](O)[C@@H](O)[C@H](C)O2)O)O1 GZSOSUNBTXMUFQ-YFAPSIMESA-N 0.000 description 2
- 229960004352 diosmin Drugs 0.000 description 2
- IGBKNLGEMMEWKD-UHFFFAOYSA-N diosmin Natural products COc1ccc(cc1)C2=C(O)C(=O)c3c(O)cc(OC4OC(COC5OC(C)C(O)C(O)C5O)C(O)C(O)C4O)cc3O2 IGBKNLGEMMEWKD-UHFFFAOYSA-N 0.000 description 2
- DTGKSKDOIYIVQL-UHFFFAOYSA-N dl-isoborneol Natural products C1CC2(C)C(O)CC1C2(C)C DTGKSKDOIYIVQL-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- VUYDGVRIQRPHFX-UHFFFAOYSA-N hesperidin Natural products COc1cc(ccc1O)C2CC(=O)c3c(O)cc(OC4OC(COC5OC(O)C(O)C(O)C5O)C(O)C(O)C4O)cc3O2 VUYDGVRIQRPHFX-UHFFFAOYSA-N 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 206010070834 Sensitisation Diseases 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000001784 detoxification Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 239000002917 insecticide Substances 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 150000004045 organic chlorine compounds Chemical class 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- -1 parts Substances 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000008313 sensitization Effects 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Apparatus For Disinfection Or Sterilisation (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Sorption (AREA)
- Cleaning Or Drying Semiconductors (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は食品、医薬品、電子・精密工業等における原材
料、部品、中間製品、包装・輸送資材等の物品を洗浄浄
化し、歩留を低下させることなく、製品の品質の向上を
計ることのてきる物品の洗浄浄化装置に関する。Detailed Description of the Invention [Industrial Field of Application] The present invention is used to clean and purify articles such as raw materials, parts, intermediate products, packaging and transportation materials in food, medicine, electronics and precision industries, etc., and reduce yield. The present invention relates to an article cleaning and purifying device that can improve the quality of products without causing any damage.
[従来の技術]
従来、物品の洗浄浄化は機械的な摩擦力、洗剤、酸化剤
、殺菌・殺虫剤等の化学薬品の化学反応力や温水、熱水
、蒸気、紫外線等の物理力か単独又は多段に更にはそれ
等を複数種類組み合わせ、複雑な操作の下で長時間掛け
、多量の洗浄水を使いなから行われている。[Conventional technology] Conventionally, cleaning and purification of articles has been carried out using mechanical frictional force, chemical reaction force of chemicals such as detergents, oxidizers, sterilizers and insecticides, and physical force such as hot water, hot water, steam, and ultraviolet rays. Or, it is performed in multiple stages or in a combination of multiple types, requiring complicated operations for a long time, and using a large amount of washing water.
又、オゾン水を使用して、物品を洗浄浄化することも試
みられている。Also, attempts have been made to use ozonated water to clean and purify articles.
[発明か解決しようとする課題]
上記従来の方法で物品を充分に洗浄浄化するには、機械
的浄化工程、化学的浄化工程、物理的浄化工程を複数、
多段に組み合わせることか必要となり、実際には装置が
大型化し、設備費が過大となり、洗浄に使用される洗浄
水中の殺菌剤、中和剤等の化学薬品類等の洗剤の種類や
洗浄水の液量やエネルキー消費量及び所要時間が増大し
、人手が掛り、歩留りも低下するばかりでは無く、排水
の水量負荷、水質負荷量等の公害対策費も増大すること
から、多くの工程が省略され勝ちとなり、化学薬品、副
反応物質等の残留、生成物の洗浄不足による物品の品質
低下・劣化、歩留りの低下等の問題たけてなく環境汚染
さえ起している。[Problem to be solved by the invention] In order to sufficiently wash and purify an article using the above conventional method, a plurality of mechanical purification steps, chemical purification steps, and physical purification steps are required.
In reality, the equipment becomes larger and the equipment cost becomes excessive, and the types of detergents such as disinfectants, neutralizers, etc. Not only does this increase the amount of liquid, energy consumption, and time required, requires more manpower, and reduces yield, but it also increases the cost of pollution control measures such as wastewater volume load and water quality load, so many processes are omitted. However, there are numerous problems such as residual chemicals and side-reactants, poor product quality and deterioration due to insufficient cleaning of products, and decreased yields, and even environmental pollution.
又、従来技術では、特に蛋白質や油脂等の不純物質か残
留し易いという問題点があった。Furthermore, the conventional technology has a problem in that impurities such as proteins and fats and oils tend to remain.
更に又、オゾン水を物品の洗浄、浄化に使用すると、オ
ゾン臭か物品に付着残留したり、これを洗浄によって除
去しようとすると多量の洗浄水な必要としたり、洗浄に
長時間を要するとか、或は排オゾンを無害化処理するた
めの装置か必要となり、多大の費用と手間を要するとい
う問題点かあった。Furthermore, when ozonated water is used for cleaning and purifying items, ozone odor may remain on the items, and attempting to remove this by cleaning requires a large amount of cleaning water or takes a long time to clean. Another problem is that it requires a device to detoxify the exhausted ozone, which requires a great deal of cost and effort.
本発明は、前述した従来技術の問題点を解消し、物品に
付着している不純物を短時間で容易に除去するとともに
、物品の洗浄浄化に使用する液量な減少せしめ、公害問
題を解決し、品質を損なうことなく高い歩留りを維持し
なから物品のコンタミネーション防止、サニタリイ化、
純度を向上させ得る物品の洗浄浄化装置を提供すること
を目的としている。The present invention solves the above-mentioned problems of the prior art, easily removes impurities attached to articles in a short time, reduces the amount of liquid used for cleaning and purifying articles, and solves the problem of pollution. , maintain high yields without compromising quality, prevent contamination of products, make them sanitary,
It is an object of the present invention to provide a cleaning and purifying device for articles that can improve purity.
[課題を解決するための手段]
上記課題を達成するために、本発明においては、高濃度
オゾンガスを水に溶解させて濃度の大きいオゾン水を製
造する濃厚オゾン水製造装置と、比較的汚れの少ない用
水を流動させなから紫外線とオゾンの作用により酸化減
菌して無菌水な製造する無菌水製造装置と、上記濃度の
大きいオゾン水な製造する際排出されたオゾンを無菌水
製造装置に供給する手段と、濃厚オゾン水製造装置で製
造された濃度の大きいオゾン水及び無菌水製造装置て製
造された無菌水を物品洗浄浄化槽に供給する手段とから
成る物品の洗浄浄化装置を使用して物品を洗浄浄化する
。[Means for Solving the Problems] In order to achieve the above-mentioned problems, the present invention provides a concentrated ozone water production device that dissolves highly concentrated ozone gas in water to produce highly concentrated ozonated water, and a relatively dirt-free ozone water production device. A sterile water production device that produces sterile water by oxidizing and sterilizing it by the action of ultraviolet rays and ozone without flowing a small amount of water, and supplying the ozone discharged during the production of highly concentrated ozone water to the sterile water production device. and a means for supplying highly concentrated ozonated water produced by the concentrated ozone water production equipment and sterile water produced by the sterile water production equipment to an article washing septic tank. Clean and purify.
又、無菌水製造装置て製造された無菌水を濾過する手段
を設ける。Further, a means for filtering the sterile water produced by the sterile water production apparatus is provided.
又、無菌水の濾過手段として直列に配設された砂濾過装
置及び活性炭濾過装置を使用する。Furthermore, a sand filtration device and an activated carbon filtration device arranged in series are used as sterile water filtration means.
[作 用]
本発明においては、致方ppmの濃度のオゾンカスを水
に溶解させて10+ng/1以上の濃度の大きいオゾン
水を製造する遣厚オゾン水製造装置から供給される濃度
の大きいオゾン水を物品の洗浄浄化に使用することによ
り、物品に付着している蛋白質や油脂を短時間て分解、
可溶化して除去する。[Function] In the present invention, ozone water with a high concentration is supplied from a thick ozone water production device that dissolves ozone scum with a concentration of 1 ppm in water to produce ozone water with a high concentration of 10+ng/1 or more. By using it to clean and purify items, it can quickly break down proteins and fats and oils attached to items.
Solubilize and remove.
又、オゾンが細菌、藻類等の微生物やウィルスを殺菌・
不活性化し、メルカプタン、ジオスミン、2−メチルイ
ソボルネオール等の臭気物質を分解し、トリへロメタン
、トリクロルエチレン等の有害物質を無毒化し、油脂、
蛋白質、等の高分子物質を低分子化して親木性、溶解性
、生物の分解性等を改善する。In addition, ozone sterilizes and kills microorganisms such as bacteria and algae, as well as viruses.
It inactivates, decomposes odorous substances such as mercaptan, diosmin, and 2-methylisoborneol, detoxifies harmful substances such as triheromethane and trichloroethylene, and decomposes odor substances such as mercaptan, diosmin, and 2-methylisoborneol.
By converting high-molecular substances such as proteins into low-molecular weight substances, it is possible to improve their affinity for wood, solubility, biodegradability, etc.
又、上記濃度の大きいオゾン水を製造する際排出された
オゾンを、流動している用水中に吸引溶解させながら、
紫外線とオゾンの作用により、オゾンを分解して極めて
活性の高い発生期酸素を発生させ、この酸素により当該
用水中の不純物を酸化殺菌して衛生度、安全度の高い無
菌水な製造する。In addition, while the ozone discharged during the production of the highly concentrated ozone water is suctioned and dissolved into the flowing water,
The action of ultraviolet rays and ozone decomposes ozone to generate highly active nascent oxygen, which oxidizes and sterilizes impurities in the water, producing sterile water with a high degree of hygiene and safety.
又、無菌水製造装置て製造された無菌水を濾過すること
により、無菌水中に含まれる微少な懸濁物質料除去し、
洗浄された物品の品質の向上を図る。In addition, by filtering the sterile water produced by the sterile water production equipment, minute suspended solids contained in the sterile water are removed.
Aim to improve the quality of washed items.
濾偽を直列に配設された砂濾過装置と活性炭濾過装置を
用いて行うことにより上記効果を増大させる。The above effect is increased by performing the filtration using a sand filtration device and an activated carbon filtration device arranged in series.
又、濃度の大きいオゾン水て物品を短時間て洗浄浄化し
、濤厚オゾン水製造装置て濃度の大きいオゾン水を製造
する際、排出されたオゾンを無菌水製造装置に送り、無
菌水製造装置で製造された無菌水て物品を再度洗浄する
ことにより、総洗浄水量を減少せしめ、且つ、濃度の大
きいオゾン水を製造する際、排出されるオゾンを有効に
利用し、オゾンの無害化装置を不要ならしめる。In addition, when products are washed and purified using highly concentrated ozonated water in a short period of time, and when producing highly concentrated ozonated water using the Toatsu ozonated water manufacturing equipment, the discharged ozone is sent to the sterile water manufacturing equipment. By washing the items again with the sterile water produced by the sterile water, the total amount of washing water is reduced, and when producing highly concentrated ozone water, the emitted ozone is effectively used and ozone detoxification equipment is installed. Close if unnecessary.
[実施例] 以下、図面に基づき、本発明の実施例を詳述する。[Example] Embodiments of the present invention will be described in detail below based on the drawings.
図中1は濃厚オゾン水製造装置てあり、図示はしていな
いか酸素含有ガス供給装置を備えたオゾン発生装置2、
気相オゾンモニター3、高濃度オゾンガス混合器4、オ
ゾン溶解反応装置5、オゾン水循環ポンプ6、液相オゾ
ンモニター7、オゾン水定量供給装M8で構成され、図
示していないか液温制御装置を具備している。In the figure, 1 is a concentrated ozone water production device, and an ozone generator 2 (not shown) is equipped with an oxygen-containing gas supply device.
It is composed of a gas phase ozone monitor 3, a high concentration ozone gas mixer 4, an ozone dissolution reaction device 5, an ozone water circulation pump 6, a liquid phase ozone monitor 7, and an ozone water quantitative supply device M8. Equipped with
オゾン発生装置2は、無声放電式のオゾン発生装置(図
示せず)を備え、オゾン発生装置2て発生したオゾンは
高濃度オゾンカス混合器4に送られ、オゾン水循環ポン
プ56て送給される循環水で、オゾン溶解反応装置5に
おいて溶解され、この循環により濃度の大きいオゾン水
か製造される。上述の循環水中には三方切換弁9を介し
て後述する無菌水が補給される。The ozone generator 2 is equipped with a silent discharge type ozone generator (not shown), and the ozone generated by the ozone generator 2 is sent to a high concentration ozone scum mixer 4, and then circulated by an ozone water circulation pump 56. Water is dissolved in the ozone dissolution reactor 5, and highly concentrated ozone water is produced through this circulation. Sterile water, which will be described later, is replenished into the above-mentioned circulating water via the three-way switching valve 9.
又、上記オゾン発生装置2て発生したオゾンの濃度を検
出するため気相オゾンモニター3に送られたオゾンは後
述する無菌水製造装置10へ送られる。Further, ozone sent to a gas phase ozone monitor 3 to detect the concentration of ozone generated by the ozone generator 2 is sent to a sterile water production device 10, which will be described later.
上述のようにして得られた、オゾン水循環ポンプ6によ
り循環される濃度の大きいオゾン水はバルブ11、オゾ
ン水定量供給装置8、バルブ12を介して、例えば歩留
り70%の精米を洗浄浄化する物品洗浄浄化装置13へ
送られ、物品に付着している蛋白質、脂肪等を分解して
可溶性とし除去すると共に減菌を行う。なお、濃度の大
きいオゾン水の洗浄に先立ち、無菌水等の浄水て予備洗
浄することはオゾン水による洗浄を均一に短時間て行う
のに有効である。The highly concentrated ozonated water, which is obtained as described above and circulated by the ozonated water circulation pump 6, is passed through the valve 11, the ozonated water quantitative supply device 8, and the valve 12 to produce, for example, an article for cleaning and purifying milled rice with a yield of 70%. The product is sent to the cleaning and purifying device 13, where proteins, fats, etc. adhering to the product are decomposed, made soluble, and removed, and sterilized. Note that prior to cleaning with highly concentrated ozonated water, preliminary cleaning with purified water such as sterile water is effective for uniformly cleaning with ozonated water in a short time.
物品洗浄浄化装置13から排出した排液は汚泥処理装置
(図示せず)を備えた排水処理装置14からバルブ15
を介して排出される。The wastewater discharged from the article washing and purifying device 13 is passed through a wastewater treatment device 14 equipped with a sludge treatment device (not shown) to a valve 15.
is discharged through.
この排液は、濃度の大きいオゾン水で物品に付着してい
る蛋白質、油脂等の高分子物質か分解、低分子化されて
いるので、その後の排液の生物酸化処理か極めて容易と
なり、又当該排水処理から発生ずる余剰汚泥を上記高濃
度オゾン水て処理することにより当該余剰汚泥の凝集・
脱水効果を大幅に改善することもてきる。This wastewater is decomposed and made into low-molecular weight substances such as proteins and oils attached to the products by highly concentrated ozonated water, so the subsequent biological oxidation treatment of the wastewater becomes extremely easy. By treating the excess sludge generated from the wastewater treatment with the above-mentioned highly concentrated ozone water, the excess sludge will be coagulated and
It can also greatly improve the dehydration effect.
なお、16はオゾン溶解反応装置5と液相オゾンモニタ
ー7の間に設けられたバルブ、17はバルブて、液相オ
ゾンモニター7から排出されたオゾンを後記する無菌水
製造装置10ヘオソンを送る際に使用するようになって
いる。In addition, 16 is a valve provided between the ozone dissolution reaction device 5 and the liquid phase ozone monitor 7, and 17 is a valve that is used to transfer ozone discharged from the liquid phase ozone monitor 7 to the sterile water production device 10, which will be described later. It is designed to be used for
無菌水製造装置10は、用水循環ポンプ18、排出オゾ
ン混合器19、受水槽20、主に253.7nmの紫外
線を発生させる紫外線ランプ21、透明石英製の保護管
22、ケーシング23と上記濃厚オゾン水製造装置lか
ら排出又は供給されるオゾンを供給するための、ケーシ
ング23と保護管22との間に形成された液体流路24
、セオライトを充填した砂濾過装置25、受槽26、活
性炭濾過装置27、受槽28から構成されている。The sterile water production device 10 includes a water circulation pump 18, a discharge ozone mixer 19, a water tank 20, an ultraviolet lamp 21 that mainly generates ultraviolet light of 253.7 nm, a protection tube 22 made of transparent quartz, a casing 23, and the above-mentioned concentrated ozone. A liquid flow path 24 formed between the casing 23 and the protection tube 22 for supplying ozone discharged or supplied from the water production device l
, a sand filtration device 25 filled with theolite, a receiving tank 26, an activated carbon filtration device 27, and a receiving tank 28.
前記濃厚オゾン水製造装置1のオゾン発生装置2て発生
したオゾンの一部、上述の気相オゾンモニター3から排
出されたオゾン及びオゾン溶解反応装置5から排出され
たオゾンは、オゾン濃度調整器29へ送られ、要すれば
Aて示される空気と混合した後、排出オゾン混合器19
へ送られる。A part of the ozone generated by the ozone generator 2 of the concentrated ozone water production device 1, the ozone discharged from the gas phase ozone monitor 3, and the ozone discharged from the ozone dissolution reaction device 5 are transferred to an ozone concentration regulator 29. and, if necessary, mixed with air indicated as A, the discharge ozone mixer 19
sent to.
排出オゾン混合器19には用水循環ポンプ18によって
、受水槽20から供給された循環水か送られ、オゾンを
含む気体と混合して無菌水か製造される。なお、Bは受
水槽20へ、地下水、工業用水等比較的汚れの少ない水
を補給する補給水である。33はバルブである。The circulating water supplied from the water receiving tank 20 is sent to the discharge ozone mixer 19 by the water circulation pump 18, and mixed with ozone-containing gas to produce sterile water. Note that B is makeup water that replenishes the water tank 20 with relatively clean water such as underground water or industrial water. 33 is a valve.
排出オゾン混合器19から送給されたオゾンは、流体通
路24に流入する水に吸引混合され紫外線ランプ21て
発生する紫外線の作用により速やかに分解し、発生期の
酸素か生成される。The ozone supplied from the discharge ozone mixer 19 is suction-mixed with the water flowing into the fluid passage 24, and is rapidly decomposed by the action of ultraviolet rays generated by the ultraviolet lamp 21, producing nascent oxygen.
この発生期の酸素と253.7mmの波長の紫外線によ
り流体通路24を流れる水は減菌浄化され、この水は三
方切換弁30を介して容量の大きい受槽20との間を循
環し、又上記三方切換弁30を介して砂濾過装置25、
受槽26、及びバルブ31を介して上述の物品洗浄浄化
装置13へ送られる。一方、受槽26からは、活性炭濾
過装置27に送られここて濾過され、洗浄水として極め
て好適なオゾンを含有しない、しかも微少な浮遊物も含
まない無菌水か得られる。The water flowing through the fluid passage 24 is sterilized and purified by this nascent oxygen and ultraviolet rays with a wavelength of 253.7 mm, and this water is circulated between the large-capacity receiving tank 20 and the above-mentioned water via the three-way switching valve 30. sand filter device 25 via a three-way switching valve 30;
It is sent to the above-mentioned article washing and purifying device 13 via the receiving tank 26 and the valve 31. On the other hand, from the receiving tank 26, the water is sent to an activated carbon filtration device 27, where it is filtered to obtain sterile water that does not contain ozone and does not contain even the slightest suspended matter, which is extremely suitable as cleaning water.
こめ無菌水は受槽28からハルツ32を′介して物品洗
浄浄化装置13へ送られ、濃度の大きいオゾン水て洗浄
された物品をゆすぎ、仕上洗浄し、この物品に残留して
いるオゾンを完全に除去する。なお、受水槽20中の無
菌水は、パルプ34を介して、直接物品洗浄浄化装置1
3へ送ることもてきる。The sterile water is sent from the receiving tank 28 to the article washing and purifying device 13 via the Harutsu 32', where the articles washed with highly concentrated ozone water are rinsed and finished washed to completely remove the ozone remaining in the articles. Remove. The sterile water in the water tank 20 is directly supplied to the article washing and purifying device 1 via the pulp 34.
You can also send it to 3.
なお、オゾン及び紫外線の作用により減菌浄化された無
菌水は、物品を濃度の大きいオゾン水て洗浄する前の、
物品の予備洗浄液として、濾過工程を経ることなく使用
することがてきる。In addition, sterile water that has been sterilized and purified by the action of ozone and ultraviolet rays should be used before washing items with highly concentrated ozone water.
It can be used as a pre-washing liquid for articles without going through a filtration process.
又、図示していないが必要に応じてイオン交換装置、限
界濾過膜装置、逆浸透膜装置を設けても良い。Further, although not shown, an ion exchange device, an ultrafiltration membrane device, and a reverse osmosis membrane device may be provided as necessary.
[発明の効果]
本発明の物品の洗浄浄化装置は、次のような優れた効果
を有する。[Effects of the Invention] The article cleaning and purifying apparatus of the present invention has the following excellent effects.
(1)酸化・殺菌力の極めて強いオゾン濃度の大きい濃
厚オゾン水により物品に付着・結合した不純物を数秒〜
数分間の短時間て分解・改質・殺菌し物品自体を殆ど損
傷・変質させることなく脱色・脱臭・漂白・精製して高
い歩留りで物品の品質向上を計れる。(1) Concentrated ozonated water with a high ozone concentration that has extremely strong oxidizing and sterilizing power removes impurities attached to and bonded to items within a few seconds.
It can be decomposed, modified, and sterilized in a short period of a few minutes, and the quality of the product can be improved with a high yield by decolorizing, deodorizing, bleaching, and refining the product without damaging or deteriorating the product itself.
(2)紫外線とオゾンを併用して製造された無菌水を濃
厚オゾン水の原水や予備洗浄水に使うので用水に起因す
る不純物の酸化に消費されるオゾンのロスが無い。(2) Since sterile water produced using a combination of ultraviolet rays and ozone is used as raw water for concentrated ozonated water and pre-wash water, there is no loss of ozone consumed by oxidation of impurities caused by service water.
(3)無菌水は、遊離塩素が紫外線の増感作用を受けて
いるために分解されているのて有害な有機塩素化合物の
生成や発臭は起こらす、又可溶性の鉄やマンガンは不溶
性塩になっているのてセオライト充填の砂濾過装置て処
理することにより簡単に、鉄分か非常に少なくマンガン
分不検出の水か製造でき、更にこれを活性炭濾過装置で
処理することにより物品のゆすぎ・仕上洗浄水や製品自
体の希釈・充填水等にも使える高純度の水を得ることが
できる。更に、純水装置で処理することにより極めて高
品質の純水をつることもてきる。このように本発明の装
置によるときは適宜必要に応して各種の純度の無菌水を
低負荷、低コストで順次製造てきる。(3) In sterile water, free chlorine is decomposed due to the sensitization effect of ultraviolet rays, resulting in the formation of harmful organic chlorine compounds and odor, and soluble iron and manganese are insoluble salts. By processing the water with a ceolite-filled sand filter, it is possible to easily produce water with very little iron and no detectable manganese.Furthermore, by processing this water with an activated carbon filter, it can be used for rinsing items. You can obtain high-purity water that can be used as finishing wash water and water for diluting and filling the product itself. Furthermore, extremely high quality pure water can be produced by treating it with a water purifier. In this way, when the apparatus of the present invention is used, sterile water of various purity can be sequentially produced with low load and low cost as required.
(4)排オゾン処理が必要なく、発生させたオゾンは有
効に利用てき、排水の水量・水質負荷も軽減されるので
、従来法の浄化に比べ経済的である。(4) There is no need for waste ozone treatment, the ozone generated can be used effectively, and the load on the amount and quality of wastewater is reduced, making it more economical than conventional purification methods.
図面は、本発明の物品の洗浄浄化装置を説明するための
回路図て、図中1は濃厚オゾン水製造装置、2はオゾン
発生装置、3は気相オゾンモニタ、4は高濃度オゾンガ
ス混合器、5はオゾン溶解反尤装鐙、6はオゾン水循環
ポンプ、7は液相オゾンモニター、8はオゾン水定量供
給装置、9三方切換弁、11は無菌水製造装置、11゜
12はハルツ、13は物品洗浄浄化装置、14は排水処
理装置、15,16.17はバルブ、18は用水循環ポ
ンプ、19は排出オゾン混合器、20は受水槽、21は
紫外線ランプ、22は保護管、23はケーシング、24
は流体通路、25は砂濾過装置、26は受槽、27は活
性炭濾過装置、28は受槽、29はオゾン濃度調整器、
30は三方切換弁、31,32,33.34はハルツを
示す。The drawing is a circuit diagram for explaining the article cleaning and purification apparatus of the present invention, in which 1 is a concentrated ozone water production device, 2 is an ozone generator, 3 is a gas phase ozone monitor, and 4 is a high concentration ozone gas mixer. , 5 is an ozone dissolution reactor stirrup, 6 is an ozone water circulation pump, 7 is a liquid phase ozone monitor, 8 is an ozone water constant supply device, 9 is a three-way switching valve, 11 is a sterile water production device, 11゜12 is Harz, 13 14 is an article washing purification device, 14 is a wastewater treatment device, 15, 16, 17 are valves, 18 is a water circulation pump, 19 is a discharge ozone mixer, 20 is a water tank, 21 is an ultraviolet lamp, 22 is a protection tube, 23 is casing, 24
is a fluid passage, 25 is a sand filtration device, 26 is a receiving tank, 27 is an activated carbon filtration device, 28 is a receiving tank, 29 is an ozone concentration regulator,
30 is a three-way switching valve, and 31, 32, 33, and 34 are Harz.
Claims (3)
オゾン水を製造する濃厚オゾン水製造装置と、比較的汚
れの少ない用水を流動させながら紫外線とオゾンの作用
により酸化減菌して無菌水を製造する無菌水製造装置と
、上記濃度の大きいオゾン水を製造する際排出されたオ
ゾンを無菌水製造装置に供給する手段と、濃厚オゾン水
製造装置で製造された濃度の大きいオゾン水及び無菌水
製造装置で製造された無菌水を物品洗浄浄化槽に供給す
る手段とから成る物品の洗浄浄化装置。(1) Concentrated ozone water production equipment that produces highly concentrated ozone water by dissolving highly concentrated ozone gas in water, and sterile water that is oxidized and sterilized by the action of ultraviolet rays and ozone while flowing relatively clean water. a sterile water production device for producing sterile water; An apparatus for cleaning and purifying articles, comprising means for supplying sterile water produced by the water production apparatus to an article washing and septic tank.
段を備えた請求項1記載の物品の洗浄浄化装置。(2) The apparatus for cleaning and purifying articles according to claim 1, further comprising means for filtering the sterile water produced by the sterile water production apparatus.
装置及ひ活性炭濾過装置よりなる請求項2記載の物品の
洗浄浄化装置。(3) The article cleaning and purifying apparatus according to claim 2, wherein the means for filtering the sterile water comprises a sand filter device and an activated carbon filter device arranged in series.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1023793A JPH02203992A (en) | 1989-02-03 | 1989-02-03 | Device for washing and purifying article |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1023793A JPH02203992A (en) | 1989-02-03 | 1989-02-03 | Device for washing and purifying article |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02203992A true JPH02203992A (en) | 1990-08-13 |
Family
ID=12120203
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1023793A Pending JPH02203992A (en) | 1989-02-03 | 1989-02-03 | Device for washing and purifying article |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02203992A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03229416A (en) * | 1990-02-02 | 1991-10-11 | Rohm Co Ltd | Method of sterilization washing of circulation route of pure water for washing in semiconductor manufacture |
WO1994024043A1 (en) * | 1993-04-14 | 1994-10-27 | Wada, Tetsuro | Method and apparatus for ozone decomposition by stimulated emission of electromagnetic wave |
US5422019A (en) * | 1994-02-23 | 1995-06-06 | Carman; Lyle | Method for removing contaminants from industrial cleaning systems |
JP2002096030A (en) * | 2000-09-26 | 2002-04-02 | Shibaura Mechatronics Corp | Treating device using nozzle |
JP2014195788A (en) * | 2013-03-29 | 2014-10-16 | 三浦工業株式会社 | Ultraviolet sterilization system |
JP2017017183A (en) * | 2015-07-01 | 2017-01-19 | 東京エレクトロン株式会社 | Liquid container and substrate liquid processing device using same liquid container |
-
1989
- 1989-02-03 JP JP1023793A patent/JPH02203992A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03229416A (en) * | 1990-02-02 | 1991-10-11 | Rohm Co Ltd | Method of sterilization washing of circulation route of pure water for washing in semiconductor manufacture |
WO1994024043A1 (en) * | 1993-04-14 | 1994-10-27 | Wada, Tetsuro | Method and apparatus for ozone decomposition by stimulated emission of electromagnetic wave |
US5422019A (en) * | 1994-02-23 | 1995-06-06 | Carman; Lyle | Method for removing contaminants from industrial cleaning systems |
JP2002096030A (en) * | 2000-09-26 | 2002-04-02 | Shibaura Mechatronics Corp | Treating device using nozzle |
JP2014195788A (en) * | 2013-03-29 | 2014-10-16 | 三浦工業株式会社 | Ultraviolet sterilization system |
JP2017017183A (en) * | 2015-07-01 | 2017-01-19 | 東京エレクトロン株式会社 | Liquid container and substrate liquid processing device using same liquid container |
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