JPH10277541A - Zeolite type water purifying agent - Google Patents
Zeolite type water purifying agentInfo
- Publication number
- JPH10277541A JPH10277541A JP10391497A JP10391497A JPH10277541A JP H10277541 A JPH10277541 A JP H10277541A JP 10391497 A JP10391497 A JP 10391497A JP 10391497 A JP10391497 A JP 10391497A JP H10277541 A JPH10277541 A JP H10277541A
- Authority
- JP
- Japan
- Prior art keywords
- water
- zeolite
- purification agent
- water purification
- based water
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 123
- 239000010457 zeolite Substances 0.000 title claims abstract description 64
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 63
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 62
- 239000012629 purifying agent Substances 0.000 title claims abstract description 11
- 239000010865 sewage Substances 0.000 claims abstract description 27
- 239000000126 substance Substances 0.000 claims abstract description 25
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 14
- 239000011707 mineral Substances 0.000 claims abstract description 14
- 239000010440 gypsum Substances 0.000 claims abstract description 12
- 229910052602 gypsum Inorganic materials 0.000 claims abstract description 12
- 239000002245 particle Substances 0.000 claims abstract description 11
- 239000000843 powder Substances 0.000 claims abstract description 10
- 239000000203 mixture Substances 0.000 claims abstract description 9
- 150000004683 dihydrates Chemical class 0.000 claims abstract description 6
- 238000000746 purification Methods 0.000 claims description 46
- 239000003795 chemical substances by application Substances 0.000 claims description 35
- 238000005345 coagulation Methods 0.000 claims description 8
- 230000015271 coagulation Effects 0.000 claims description 8
- 238000004062 sedimentation Methods 0.000 claims description 8
- 238000002156 mixing Methods 0.000 claims description 4
- ZOMBKNNSYQHRCA-UHFFFAOYSA-J calcium sulfate hemihydrate Chemical compound O.[Ca+2].[Ca+2].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O ZOMBKNNSYQHRCA-UHFFFAOYSA-J 0.000 claims description 3
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical group [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 2
- 235000019353 potassium silicate Nutrition 0.000 claims description 2
- 241001465754 Metazoa Species 0.000 claims 2
- 239000011148 porous material Substances 0.000 claims 1
- 235000020188 drinking water Nutrition 0.000 abstract description 26
- 239000003651 drinking water Substances 0.000 abstract description 26
- 230000000694 effects Effects 0.000 abstract description 8
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 abstract description 5
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000013049 sediment Substances 0.000 abstract description 3
- 238000004065 wastewater treatment Methods 0.000 abstract description 3
- 239000000356 contaminant Substances 0.000 abstract 1
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 14
- 239000011575 calcium Substances 0.000 description 14
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 12
- 229910052791 calcium Inorganic materials 0.000 description 12
- 235000010755 mineral Nutrition 0.000 description 12
- 235000013339 cereals Nutrition 0.000 description 11
- 239000010802 sludge Substances 0.000 description 10
- 238000001179 sorption measurement Methods 0.000 description 9
- 230000009471 action Effects 0.000 description 7
- 229910000019 calcium carbonate Inorganic materials 0.000 description 7
- 229910021645 metal ion Inorganic materials 0.000 description 7
- 239000011574 phosphorus Substances 0.000 description 7
- 229910052698 phosphorus Inorganic materials 0.000 description 7
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- -1 silicate ions Chemical class 0.000 description 5
- 229910052710 silicon Inorganic materials 0.000 description 5
- 239000010703 silicon Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 239000000395 magnesium oxide Substances 0.000 description 4
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 230000002195 synergetic effect Effects 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 229910021532 Calcite Inorganic materials 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 229910052793 cadmium Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 239000010840 domestic wastewater Substances 0.000 description 3
- 229910052753 mercury Inorganic materials 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 235000015097 nutrients Nutrition 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 241000251468 Actinopterygii Species 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 241000238578 Daphnia Species 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 239000008280 blood Substances 0.000 description 2
- 210000004369 blood Anatomy 0.000 description 2
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000010730 cutting oil Substances 0.000 description 2
- 239000012024 dehydrating agents Substances 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 230000035622 drinking Effects 0.000 description 2
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 2
- 239000000976 ink Substances 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 2
- 150000003018 phosphorus compounds Chemical class 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000010909 process residue Substances 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 235000015170 shellfish Nutrition 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 241000192700 Cyanobacteria Species 0.000 description 1
- 206010012289 Dementia Diseases 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 241000237858 Gastropoda Species 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 241001045988 Neogene Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- WBLXMRIMSGHSAC-UHFFFAOYSA-N [Cl].[Cl] Chemical compound [Cl].[Cl] WBLXMRIMSGHSAC-UHFFFAOYSA-N 0.000 description 1
- 230000004931 aggregating effect Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000037429 base substitution Effects 0.000 description 1
- 230000033558 biomineral tissue development Effects 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- YWEUIGNSBFLMFL-UHFFFAOYSA-N diphosphonate Chemical compound O=P(=O)OP(=O)=O YWEUIGNSBFLMFL-UHFFFAOYSA-N 0.000 description 1
- FZFYOUJTOSBFPQ-UHFFFAOYSA-M dipotassium;hydroxide Chemical compound [OH-].[K+].[K+] FZFYOUJTOSBFPQ-UHFFFAOYSA-M 0.000 description 1
- NTGONJLAOZZDJO-UHFFFAOYSA-M disodium;hydroxide Chemical compound [OH-].[Na+].[Na+] NTGONJLAOZZDJO-UHFFFAOYSA-M 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 210000000936 intestine Anatomy 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 101150091879 neo gene Proteins 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000004045 organic chlorine compounds Chemical class 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- DLYUQMMRRRQYAE-UHFFFAOYSA-N phosphorus pentoxide Inorganic materials O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Water Treatment By Sorption (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、飲料水や汚水等
も浄化するゼオライトを主成分とする水質浄化剤に係
り、特に飲料水の有害物質を除去し、また汚水を浄化処
理するのに好適なゼオライト系水質浄化剤に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purification agent containing zeolite as a main component which purifies drinking water and sewage, and is particularly suitable for removing harmful substances from drinking water and purifying sewage. A novel zeolite-based water purification agent.
【0002】[0002]
【従来の技術】産業の集中、大規模化による産業排水の
増大、都市への人口集中による生活排水の増大、下水道
整備の立遅れ等が原因による水質汚濁が進み、水道原
水、工業用水の汚濁が深刻な事態を招いている。元来飲
料水は生命体に良い水でなくてはならない。その条件
は、単に有害物質を含まないだけでなく、金属イオンで
あるミネラル成分を含み酸素と炭酸ガスが充分溶け込ん
でいることであり、しかも水の硬度が高過ぎず弱アルカ
リであって、水のクラスター(分子集団)がより小さい
ことである。2. Description of the Related Art Water pollution is increasing due to the concentration of industry, increase of industrial drainage due to large scale, increase of domestic wastewater due to concentration of population in cities, delay of sewerage maintenance, etc., and pollution of raw water for tap water and industrial water. But this is causing a serious situation. Naturally, drinking water must be good for living organisms. The condition is not only that it does not contain harmful substances, but also that it contains a mineral component that is a metal ion and that oxygen and carbon dioxide gas are sufficiently dissolved. Is smaller.
【0003】このような飲料水を飲むことによって、生
命体の細胞を生き生きさせ、健康な体を作り、若々しい
肌を保って老化を遅らせ、痴呆症の予防にもなる。前記
金属イオンは、カルシウム、カルシウムイオン、けい酸
イオン等であり、このイオン濃度の高い飲料水が良い飲
料水といえる。特にクラスタ−の小さい飲料水は、生命
体の酵素の働きを活発にし、腸内部の微生物の働きを活
発にさせ新陳代謝を早める。[0003] By drinking such drinking water, the cells of living organisms are brought to life, a healthy body is formed, the youthful skin is maintained, aging is delayed, and dementia is prevented. The metal ions are calcium, calcium ions, silicate ions and the like, and it can be said that drinking water having a high ion concentration is good drinking water. In particular, drinking water with a small cluster activates enzymes of living organisms, activates microorganisms in the intestine, and accelerates metabolism.
【0004】このような飲料水としては、天然の湧水等
がクラスタ−が小さく、カルシウム等の金属イオン(ミ
ネラル)を多く含んでいるため、喉ごしの柔らかな美味
しい飲料水としてペットボトル等に入れて販売されてい
るが、人工的にこのような飲料水を大量に生成するため
には高額な設備が必要になる。As such drinking water, natural spring water or the like has small clusters and contains a large amount of metal ions (minerals) such as calcium. Although it is sold in a container, expensive equipment is required to artificially produce such a large amount of drinking water.
【0005】一方、工場廃液や生活排水の流入によっ
て、河川や湖沼などはヘドロが発生して汚水となりがち
である。この汚水のヘドロは、嫌気性菌が主体となっ
て、アンモニアやメタン、硫化水素等を発生して水を汚
くする。これらの汚水は汚水処理浄化装置で化学処理さ
れ、フイルタ−等を用いて浄化されている。特に工場廃
液等に対しては、近年高度な汚水処理浄化装置の設備が
義務付けられるようになっている。[0005] On the other hand, rivers, lakes and marshes are liable to become sewage due to sludge due to inflow of factory wastewater and domestic wastewater. The sewage of this sewage is mainly composed of anaerobic bacteria, and generates ammonia, methane, hydrogen sulfide, etc., and pollutes the water. These sewage are chemically treated by a sewage treatment and purification device, and are purified using a filter or the like. In particular, in recent years, equipment for advanced sewage treatment and purification equipment has become mandatory for factory waste liquids and the like.
【0006】[0006]
【発明が解決しようとする課題】しかし、従来の飲料水
としての水道水には有害なカルキ(塩素)などが含まれ
ていて、決して最適な飲料水とは言い難いという問題が
あったし、また、海や河川、湖沼に生活排水、農薬等が
流れ込んで水中の植物栄養塩類の濃度が高まり水質が貧
栄養から富栄養に変化し、水中の窒素やリン等の栄養分
が過多となり植物プランクトン等の生物が異常繁殖し赤
潮やアオコとなり、この状態が進んでアオコが腐敗して
分解される時に酸素が消費されるので魚類が酸欠を起こ
して死に、水は悪臭を放つようになるという問題があっ
た。However, there is a problem that tap water as conventional drinking water contains harmful chlorine (chlorine) and the like, and it is difficult to say that the drinking water is optimal. In addition, domestic wastewater and pesticides flow into the sea, rivers and lakes, increasing the concentration of phytonutrients in the water, changing the water quality from oligotrophic to eutrophic, and resulting in excessive nutrients such as nitrogen and phosphorus in the water and phytoplankton, etc. The problem is that the fish grows abnormally and becomes red tide and blue water, and when this condition progresses and the blue water rots and decomposes, oxygen is consumed, so the fish die out due to lack of oxygen, and the water becomes stinking. was there.
【0007】このような飲料水や汚水に対して水質浄化
設備は莫大な高額設備を必要とし、国や地方団体でなけ
れば設備不可能であり、特に海や河川、湖沼の水質浄化
には広範囲の設備やメンテナンス等を実施しなければな
らないという問題があった。いずれにしても沈降分離は
廃水処理に於ける分離操作の主流をなしているものの、
その急速分離は専ら凝集沈殿処理メカニズムを改善する
ことによって行われており、沈降速度には限界があり、
凝集機能そのものを改善し、急速に大粒のフロックを形
成させることが出来るとは考えられていなかった。この
発明は上記した点に鑑みてなされたものであり、その目
的とするところは従来例の問題点を解消し、高額な設備
費を必要とせず、飲料水や河川、湖沼等の水質浄化を行
うゼオライトを主成分とする水質浄化剤と簡便に製造で
きる水質浄化剤とを提供するところにある。For such drinking water and sewage, water purification equipment requires enormous and expensive equipment and cannot be installed unless a national or local organization is used. In particular, water purification for the sea, rivers, lakes and marshes is widely used. There was a problem that it was necessary to carry out equipment and maintenance. In any case, sedimentation separation is the mainstream of separation operation in wastewater treatment,
The rapid separation is performed solely by improving the coagulation and sedimentation treatment mechanism, and the sedimentation speed is limited.
It was not considered that the flocculation function itself could be improved and large flocs could be rapidly formed. The present invention has been made in view of the above points, and aims at solving the problems of the conventional example, eliminating the need for expensive equipment costs, and purifying water quality of drinking water, rivers, lakes and marshes. It is an object of the present invention to provide a water purification agent containing zeolite as a main component and a water purification agent that can be easily produced.
【0008】[0008]
【課題を解決するための手段】この発明のゼオライトを
主成分とする水質浄化剤は、粉末ゼオライトを主成分と
し、これに微粒化した人畜無害の多孔物質(貝化石も含
む)と、水に溶解して水ガラスとなる非結晶質成分を含
むものと、二水石膏と可溶性無水石膏との粉末混合物と
を添加混合してなり、水に含まれた汚れ及び有害物質を
除去し、水中にミネラル成分を溶出し、水のクラスター
をより小さく生成することを特徴とする。この粉末ゼオ
ライトを主成分とする水質浄化剤は、特に飲料用水源地
の水質浄化に好適である。The water purification agent of the present invention containing zeolite as a main component is composed of powdered zeolite as a main component. A mixture containing a non-crystalline component that dissolves into water glass and a powder mixture of gypsum dihydrate and a soluble anhydrous gypsum are added and mixed to remove dirt and harmful substances contained in water, It is characterized by eluting mineral components and producing smaller water clusters. This water purification agent containing powder zeolite as a main component is particularly suitable for water purification of drinking water sources.
【0009】この発明の汚水浄化に適したゼオライト系
水質浄化剤は、粉末ゼオライト60〜80重量%と、人
畜無害の多孔物質(貝化石も含む)を粉砕し、300℃
以下の温度で乾燥し、微粉末化したこれらの物質10〜
30重量%と水溶性けい素含有物の粉体と二水石膏と可
溶性無水石膏との粉末混合物20〜40重量%とを混合
してなり、汚水の浄化力を有することを特徴とする。The zeolite-based water purifying agent suitable for purifying sewage according to the present invention is obtained by pulverizing 60 to 80% by weight of powdered zeolite and a harmless porous substance (including fossil shellfish) at 300 ° C.
These substances dried and pulverized at the following temperature
It is characterized by having 30% by weight of a powder of a water-soluble silicon-containing material, 20 to 40% by weight of a powder mixture of gypsum dihydrate and soluble anhydrite, and having the ability to purify sewage.
【0010】この発明において水質浄化剤に使用するゼ
オライトは、飲料水の水質浄化剤に使用する場合には、
ゼオライト自身は、水中にミネラル成分を溶出し、水の
クラスターをより小さく生成する能力が低いため、貝化
石粒よりも配合量が多ければよく、50重量%以上であ
ればよい。[0010] In the present invention, the zeolite used as a water purifying agent, when used as a water purifying agent for drinking water,
Since zeolite itself has a low ability to elute mineral components in water and generate smaller clusters of water, the amount of zeolite is preferably larger than that of shell fossil grains, and may be 50% by weight or more.
【0011】ゼオライトは、おもにアルミニウム、ナト
リウム、カルシウムのけい酸塩水和物で、Na+(又はK
+)のような容易に交換されるイオンをもち、水中のC
a2+やMg2+と置き換えして水の軟化作用を行うことは
周知であるが、廃水処理における吸着剤として活性炭
(有機物、色成分の除去)とともに、ゼオライトはアン
モニアの吸着剤として良く知られている。なお本発明に
いう「ゼオライト」とは、ゼオライト、モルデナイト、
クリノプチライト、合成ゼオライトなどのゼオライト系
鉱物の総称を意味する。Zeolites are mainly silicate hydrates of aluminum, sodium and calcium, Na + (or K
+ ) With easily exchangeable ions such as
It is well known that water is replaced by a 2+ or Mg 2+ to soften water. However, zeolite is well known as an adsorbent for ammonia together with activated carbon (removal of organic substances and color components) as an adsorbent in wastewater treatment. Have been. In the present invention, "zeolite" refers to zeolite, mordenite,
A general term for zeolite-based minerals such as clinoptilite and synthetic zeolite.
【0012】この発明において貝化石原料として使用す
る貝化石塊は、貝化石層を採掘したもので、この貝化石
層は、新第三期中頃(約1200万年前)に海生貝類、
特に二枚貝、巻き貝等、および、海棲生物の骨格遺骸等
が密集して埋没堆積して地下の高い圧力に伴う高温度に
よって粒状ないし細片状になって固まって形成され、地
殻変動、陸地化に伴って地上に現れたものを対象とし
た。貝化石の主成分は、炭酸カルシウムであるが、その
他に微量要素の酸化マグネシウム(MgO)や酸化第二
鉄(Fe2 P 3)など多種類の要素が含有されている。In the present invention, the shell fossil mass used as a shell fossil raw material is obtained by mining a shell fossil layer, and this shell fossil layer is composed of marine shells and marine shellfish in the middle of the Neogene period (about 12 million years ago).
In particular, bivalves, snails, etc., and skeletons of marine organisms are densely buried and deposited, and they are formed into particles or strips and solidified by the high temperature caused by high underground pressure, resulting in crustal deformation and land transformation. The ones that appeared on the ground along with were targeted. The main component of shell fossils is calcium carbonate, but also contains various elements such as magnesium oxide (MgO) and ferric oxide (Fe 2 P 3 ) as trace elements.
【0013】このようにして生成された貝化石は、貝殻
とは違って多孔質となっており、表面積が大きくて吸着
力が強く、同容積の活性炭の1/5の吸着力がある。ま
た、主成分である炭酸カルシウムは水に溶け出しやす
く、方解石の約10倍溶け出しやすい。更に、炭酸ガス
(CO2 )を含んだ水に対しては更に大きい溶解量を示
す。飲料水として適した雨水や地表水には炭酸ガスが多
く含有されているため、貝化石の飲料水浄化力は一層強
まる。The shell fossils thus produced are porous, unlike shells, have a large surface area and a high adsorption power, and have an adsorption power of 1/5 that of activated carbon of the same volume. Calcium carbonate, which is the main component, easily dissolves in water, and is about ten times as easy as calcite. Further, it shows a larger amount of dissolution in water containing carbon dioxide gas (CO 2 ). Rainwater and surface water, which are suitable as drinking water, contain a large amount of carbon dioxide, so that the purifying ability of shell fossils for drinking water is further enhanced.
【0014】飲料水用水質浄化剤は、貝化石をそのまま
使用した場合、けい素分が過分に溶け出すと独特のにお
いが出て飲用に不向きであるので、貝化石中のけい素分
を水漬工程で予め溶出し除去する。水漬工程によってカ
ルシウム分も幾分溶け出すが、けい素分の方が先に多く
溶け出すし、カルシウム分は豊富なので、有効なカルシ
ウム分を失うことはない。[0014] The water purifying agent for drinking water, when used directly as shell fossils, is unsuitable for drinking because of the unusual smell of silicon if it is excessively dissolved. Elute and remove in advance in the pickling process. Although some calcium is dissolved by the water-immersion process, silicon is dissolved more first and calcium is abundant, so that effective calcium is not lost.
【0015】この発明になる飲料水用の浄化剤中の貝化
石は、多孔質の貝化石の粒径を適度に細かくしたから、
これを飲料水に投入すると、カルキ等の有害物質の吸
着、カルシウム分等のミネラルの溶け出し、有機塩素化
合物との反応が速やかで有害物質を強力に除去し、水の
クラスタ−をより小さく生成して飲み心地のよい水と
し、しかも、長期間使用できる。The shell fossil in the purifying agent for drinking water according to the present invention has a porous shell fossil having an appropriately small particle size.
When this is put into drinking water, it absorbs harmful substances such as calcium, dissolves out minerals such as calcium, reacts quickly with organic chlorine compounds, removes harmful substances strongly, and generates smaller water clusters. It is easy to drink and can be used for a long time.
【0016】この発明になる汚水浄化用の水質浄化剤
は、粉末ゼオライトに細粒にした貝化石や二水石膏、可
溶性無水石膏を混合してあるので、その相乗作用も加わ
り、貝化石の吸着、触媒、キレート効果及び凝集特性が
特によく速やかに働き、ガスの発生を止め、急速に水中
の汚れを分離し、ヘドロを吸着、凝集して沈降する。沈
降したヘドロは炭酸カルシウムの作用により、方解石化
し始めて水底に沈殿するのであるが、この際、貝化石の
Caがゼオライト中のけい酸ナトリウムのNaと置換反
応を起こし、Naイオンが増えてコロイド状の汚れに対
する吸着、凝集作用が一層強化され、更に、石膏のSO
4 -- が汚水中の金属イオンと結合して沈降を促進する。
ヘドロ中のCd,Hg等の重金属、切削油、インク、亜
硫酸ガス等も吸収し、水のpHも6.8程度の中性とな
る。The water purification agent for purifying sewage according to the present invention is obtained by mixing powdered zeolite with finely divided shell fossils, dihydrate gypsum, and soluble anhydrous gypsum. The catalyst, the chelating effect and the coagulation properties work particularly well and quickly, stop the generation of gas, rapidly separate the dirt in the water, adsorb the sludge, coagulate and settle. The settled sludge starts to calcite and precipitate on the bottom of the water due to the action of calcium carbonate. At this time, Ca in the shell fossils undergoes a substitution reaction with Na of sodium silicate in the zeolite, and Na ions increase to form colloids. Adsorption and coagulation of dirt are further enhanced, and gypsum SO 2
4 - to promote sedimentation bonded to the metal ions in the wastewater.
It also absorbs heavy metals such as Cd and Hg in sludge, cutting oil, ink, sulfur dioxide, etc., and the pH of water becomes neutral to about 6.8.
【0017】炭酸カルシウムは、水中に分散、溶解して
いる物を吸着し、リン化合物と反応してCaCO3 +P
化合物+H2 O→Ca(PO4 )+CO+O3 +H2 O
のように反応して活性酸素を発生させ、この活性酸素は
汚水に対する著しい殺菌作用を呈して水中の菌を減少す
る。また、水中のリンが減少し、ミジンコ、アオコ等の
栄養源を減らしてその異常増殖を防ぐ。この凝集作用に
より、パルプ廃液、食品加工廃液、血液等の処理にも用
いて有効である。Calcium carbonate adsorbs substances dispersed and dissolved in water and reacts with phosphorus compounds to produce CaCO 3 + P
Compound + H 2 O → Ca (PO 4 ) + CO + O 3 + H 2 O
To generate active oxygen, which has a significant bactericidal action on sewage and reduces bacteria in the water. In addition, the amount of phosphorus in the water is reduced, thereby reducing nutrient sources such as daphnia and blue-green algae to prevent the abnormal growth. Due to this coagulation action, it is also effectively used for treating pulp waste liquid, food processing waste liquid, blood and the like.
【0018】ゼオライトは、上記の貝化石や石膏のよう
に水中へ水質浄化に有効な成分が溶出して浄化作用を発
揮するものではないが、これらの水質浄化成分で除去で
きない上、澄水中に残留する有機物、色成分、塩素、ア
ンモニア等の悪臭成分を吸着し、かつ、水の軟化作用を
有するから、前記2者の水質浄化成分と併用することに
より、これらの水質浄化作用との相乗効果が発揮され
て、処理水質が一段と向上すると共に飲料水として品質
の向上したミネラル水を提供することができ、最近の健
康志向ブームに極めて適合した性能を有する水質浄化成
分となる。Zeolites do not exhibit a purifying action by eluting a component effective for water purification into water like the above-mentioned shell fossils and gypsum. However, zeolite cannot be removed by these water-purifying components and cannot be removed in clear water. Adsorbs residual organic substances, color components, malodorous components such as chlorine and ammonia, and has a water softening effect. Therefore, when used in combination with the above two water purification components, a synergistic effect with these water purification effects is obtained. Is exhibited, and the quality of treated water can be further improved, and mineral water with improved quality as drinking water can be provided. Thus, it is a water purification component having performance extremely suitable for recent health-oriented booms.
【0019】[0019]
【発明の実施の形態】粉末ゼオライト約50重量%、1
0mm以下の粒状に粉砕した貝化石粒を水洗後、水槽タ
ンク中で4〜18時間水に浸して放置し、けい素分を溶
出除去し、乾燥ドライヤーで100〜300℃の温度で
10〜20分乾燥し、更に編目数ミリの網を使用して3
〜5mmの粒径に選別した貝化石粒約50重量%の割合
で混合して飲料水の浄化に使用した。DETAILED DESCRIPTION OF THE INVENTION About 50% by weight of powdered zeolite, 1
After the shell fossil grains crushed into particles of 0 mm or less are washed with water, they are immersed in water for 4 to 18 hours in a water tank and left to elute and remove silicon components. After drying, use a mesh with a stitch of several millimeters.
The shell fossil grains selected to a particle size of 55 mm were mixed at a ratio of about 50% by weight and used for drinking water purification.
【0020】このようにして、製造されたゼオライトを
主成分とする水質浄化剤は、貝化石粒のカルシウム分等
のミネラルの溶け出し、貝化石粒とゼオライトとのカル
キ等の有害物質や有機塩素化合物との反応、吸着が速や
かに進み、汚水中の金属イオンとの結合とゼオライトに
よる金属イオンの交換作用との相乗効果による金属イオ
ンの除去が促進され、更に、貝化石粒とゼオライトによ
る脱臭作用の相乗効果により、口当たりの良いミネラル
分の豊富な良質のミネラル水を簡単迅速に得ることがで
きる。The water purifying agent containing zeolite as a main component thus produced dissolves minerals such as calcium in shell fossil grains, harmful substances such as calcium between shell fossil grains and zeolite, and organic chlorine. The reaction and adsorption with the compound proceed quickly, the removal of metal ions is promoted by the synergistic effect of the binding with the metal ions in the sewage and the exchange of the metal ions by the zeolite, and the deodorization by the shell fossil grains and the zeolite By the synergistic effect of the present invention, it is possible to easily and quickly obtain high-quality mineral water rich in minerals having a good taste.
【0021】次に、ゼオライト系水質浄化剤の汚水浄化
の実施形態について説明する。粉末ゼオライトと、上記
の方法で粉砕して得た貝化石粒をスチームドライヤーで
ほぼ300℃以下の温度で水分含有量が8%以下になる
まで乾燥し、次いで30メッシュ以下の細粒に粉砕した
貝化石粒と、水溶性けい素含有物質と、二水石膏と可溶
性無水石膏とをほぼ等量ずつ混合した石膏混合物を、粉
末ゼオライト50重量%、貝化石粒20重量%、石膏混
合物30重量%の割合で混合して汚水浄化用のゼオライ
ト系水質浄化剤を得た。Next, an embodiment of purifying sewage with a zeolite water purification agent will be described. The powdered zeolite and the shell fossil grains obtained by pulverization by the above-mentioned method were dried by a steam dryer at a temperature of about 300 ° C. or less until the water content became 8% or less, and then pulverized into fine grains of 30 mesh or less. A gypsum mixture in which shell fossil grains, a water-soluble silicon-containing substance, gypsum dihydrate and soluble anhydrous gypsum are mixed in approximately equal amounts, powder zeolite 50% by weight, shell fossil particles 20% by weight, gypsum mixture 30% by weight To obtain a zeolite-based water purification agent for sewage purification.
【0022】このゼオライト系水質浄化剤をヘドロなど
が発生した汚水に入れると、貝化石から溶け出した炭酸
カルシウムが汚水中のリン化合物と反応して水中のリン
を減少し、活性酸素を発生し、低圧低温型の貝化石構造
により汚水中の元素群を再配位させて元素群の触媒やキ
レ−ト効果で菌を減少させ、ガスの発生を止めヘドロの
汚れを分解し沈殿させることができる。二水石膏、可溶
性無水石膏とゼオライトは、水の汚れを素早く分離し、
同時に貝化石はヘドロを吸着し凝集して水中で鉱物化の
中間状態となり、貝化石の炭酸カルシウムの作用によっ
て方解石化し水底に沈んで固まる。この場合、ヘドロに
含まれている重金属や切削油、インク、重油燃焼時の煙
突から出た亜硫酸ガス等を吸収しpHもほぼ6.8程度
の中性となる。When this zeolite-based water purification agent is added to sewage generated by sludge, calcium carbonate dissolved from fossil shells reacts with phosphorus compounds in the sewage to reduce phosphorus in the water and generate active oxygen. The low pressure and low temperature shell fossil structure relocates the elements in the sewage to reduce the number of bacteria by the catalyst and chelating effect of the elements, stops the generation of gas, and decomposes and precipitates sludge dirt. it can. Gypsum, soluble anhydrous gypsum and zeolite quickly separate water stains,
At the same time, the shell fossils absorb sludge and coagulate to become an intermediate state of mineralization in water, and calcite by the action of calcium carbonate of the shell fossils and settle to the bottom of the water. In this case, the sludge absorbs heavy metals, cutting oil, ink, sulfur dioxide gas emitted from the chimney at the time of heavy oil combustion, and the pH of the sludge becomes about 6.8.
【0023】また、ゼオライト系水質浄化剤を池などに
投入して撹拌すると、ゼオライト系水質浄化剤中の貝化
石から、上述の化学反応により、酸素が発生して池の水
の上層水温と水底の水温が均等化する現象が現れ、ゼオ
ライト系水質浄化剤は水に分散又は溶解している物質が
有機質又は無機質にかかわらず急激にこれらを吸着し沈
殿するため、僅か30秒程で水がきれいになる。その結
果、水中の栄養分が減って池の中のミジンコやアオコの
異常増殖を抑える。When the zeolite-based water purification agent is charged into a pond or the like and stirred, oxygen is generated from the fossils in the zeolite-based water purification agent by the above-described chemical reaction, and the upper water temperature and the water bottom of the pond water are generated. The phenomenon of water temperature equalization appears, and the zeolite-based water purification agent rapidly adsorbs and precipitates substances dispersed or dissolved in water regardless of whether they are organic or inorganic. Become. As a result, nutrients in the water are reduced, and the abnormal growth of daphnia and blue water in the pond is suppressed.
【0024】更に、ゼオライト系水質浄化剤中の貝化石
からの炭酸カルシウムは汚水中に含まれたリン化合物と
反応してリン酸カルシウム(CaPO4 )になって富栄
養源のリンを激減させる。また、更に、ゼオライト系水
質浄化剤は化合しないリン化合物を吸着してリン化合物
を除去することができる。このようにゼオライト系水質
浄化剤の凝集作用を利用してパルプ廃液や糞尿、食品加
工廃液、血液等の汚水処理を行うことができ、処理後の
水は中性となり、多量に使用してもpHの変動がない。Further, calcium carbonate from shell fossils in the zeolite-based water purification agent reacts with a phosphorus compound contained in the sewage to become calcium phosphate (CaPO 4 ), which drastically reduces phosphorus as a eutrophic source. Further, the zeolite-based water purification agent can remove a phosphorus compound by adsorbing a phosphorus compound which is not combined. Thus, sewage treatment of pulp waste liquid, manure, food processing waste liquid, blood, etc. can be performed by utilizing the aggregating action of the zeolite-based water purification agent, and the treated water becomes neutral and can be used in large quantities. There is no change in pH.
【0025】なお、この水質浄化剤に使用したゼオライ
ト(大平洋工業(株))製の分析結果は、次の成分から
なることを示した。 ゼオライト成分(大平洋) 二酸化けい素(SiO2 ) 69.1% 酸化第二鉄(Fe2 O3 ) 0.48% 酸化マグネシウム(MgO) 0.25% 酸化カリウム(K2 O) 1.29% 水素イオン(pH) 9.7 酸化アルミニウム(Al2 O3 ) 10.8% 酸化カルシウム(CaO) 2.02% 酸化ナトリウム(NaO) 2.25% 五酸化リン(P2 O5 ) 0.04% 塩基置換容量(CEC) 118.2meq /100gThe analysis results of zeolite (manufactured by Taiheiyo Kogyo Co., Ltd.) used for this water purification agent showed that it consisted of the following components. Zeolite component (Pacific Ocean) Silicon dioxide (SiO 2 ) 69.1% Ferric oxide (Fe 2 O 3 ) 0.48% Magnesium oxide (MgO) 0.25% Potassium oxide (K 2 O) 1.29 % Hydrogen ion (pH) 9.7 aluminum oxide (Al 2 O 3 ) 10.8% calcium oxide (CaO) 2.02% sodium oxide (NaO) 2.25% phosphorus pentoxide (P 2 O 5 ) 04% base substitution capacity (CEC) 118.2meq / 100g
【0026】上記のようにゼオライト系水質浄化剤の吸
着力は非常に強力で、公害源とされているカドミウムや
水銀等の吸着において大きな威力を発揮することができ
る。実験結果によると、カドミウム吸着量は2.3mg
〜27.0mg/g、水銀吸着量は20.0mg〜2
4.0mg/gという値が測定された。この場合、単な
るイオン交換でなく不溶液物質として凝集する。As described above, the adsorption power of the zeolite-based water purification agent is extremely strong, and can exert a great power in the adsorption of cadmium, mercury and the like, which are pollutants. According to the experimental results, the amount of cadmium adsorbed was 2.3 mg.
~ 27.0mg / g, mercury adsorption amount is 20.0mg ~ 2
A value of 4.0 mg / g was measured. In this case, it aggregates as an insoluble substance, not just ion exchange.
【0027】このようにゼオライト系水質浄化剤は如何
なる汚水に対しても強力な浄化作用を発揮して汚水処理
することができる。なお、この発明における何れの用途
のゼオライト系水質浄化剤も、その粒径は用途、使用期
間等に応じて適宜選択するとよい。粒径が適宜のサイズ
範囲のものを混在させると、水に入れたとき、先ず細か
い貝化石粒の多孔質部に水が浸入して速やかに反応し、
大粒の貝化石粒の多孔質部には緩やかに反応するからゼ
オライト系水質浄化剤を使用できる期間が長くなる。こ
の発明に用いたゼオライトは、上記したようにイオン交
換能か吸着作用に由来する汚れ分離作用があり、貝化石
との相乗効果が得られる。As described above, the zeolite-based water purification agent exerts a strong purification effect on any wastewater and can treat wastewater. The particle size of the zeolite-based water purification agent for any use in the present invention may be appropriately selected according to the use, the period of use, and the like. If the particle size is mixed with an appropriate size range, when it is put in water, water will first penetrate into the porous part of the fine shell fossil grains and react quickly,
Since the porous part of the large shell fossil grains reacts slowly, the period during which the zeolite-based water purification agent can be used is prolonged. As described above, the zeolite used in the present invention has a dirt-separating action derived from an ion-exchange ability or an adsorbing action, and has a synergistic effect with shell fossils.
【0028】また、特に第2の実施形態で詳述した汚水
処理用のゼオライト系水質浄化剤は、同じ吸着、凝集、
沈降作用により、土砂が混入した泥水、例えば、赤土の
泥水、水を多く含んだヘドロ、擁壁工事の斜面の土砂
流、トンネル工事の排水等の強力な脱水剤としても使用
できる。即ち、このような泥水に汚水処理用の貝化石水
質浄化剤(脱水剤)を散布して泥水を撹拌すると、水分
が速やかに分離して、土砂を固めることができ、水の排
出と、土砂の搬出あるいはその場での安定した土砂の使
用を可能とするとともに、土砂流出による海洋等の環境
汚染を防止することができる。なお、この脱水剤を散布
したまま泥水を撹拌しなくても、時間はかかるけれど
も、脱水は進行して行き、水の分離と土砂の沈降、脱水
が行われる。Further, the zeolite-based water purification agent for sewage treatment described in detail in the second embodiment has the same adsorption, coagulation,
Due to the sedimentation action, it can be used as a powerful dewatering agent for muddy water mixed with earth and sand, for example, muddy water of red soil, sludge containing a lot of water, sediment flow on slopes of retaining wall construction, and drainage of tunnel construction. That is, when a muddy water is stirred by mixing a fossil water purification agent (a dehydrating agent) for sewage treatment with such muddy water, water can be quickly separated and the soil can be hardened. And stable use of earth and sand at the site can be achieved, and environmental pollution of the ocean and the like due to earth and sand outflow can be prevented. It is to be noted that although it takes a long time even if the muddy water is not stirred while the dehydrating agent is sprayed, the dehydration proceeds, and the separation of water, sedimentation of sediment, and dehydration are performed.
【0029】[0029]
【発明の効果】この発明に係るゼオライト系水質浄化剤
は、前述のように、ゼオライトと貝化石の吸着特性によ
って水道水に含まれているカルキを瞬時に除去し、水に
含まれている人体に有害な重金属を吸着する。また、水
が酸化している時にはアルカリ水に変え、貝化石に含ま
れているカルシウムなど多種類のミネラル分が水に溶出
され純良なミネラル分が多く含有した美味しい健康的な
飲料水を得ることができるという効果がある。更に、こ
のようにして生成した飲料水は水のクラスタ−が小さく
なって飲み易く、米飯やコ−ヒなどに使用しても美味し
い飲食物を得ることができる。As described above, the zeolite-based water purifying agent according to the present invention instantly removes calcium contained in tap water due to the adsorption characteristics of zeolite and shell fossils, and removes human body contained in water. Adsorbs harmful heavy metals. In addition, when water is oxidized, replace it with alkaline water and obtain various kinds of minerals such as calcium contained in shell fossils eluted in the water to obtain delicious healthy drinking water containing a lot of pure minerals There is an effect that can be. Further, the drinking water thus produced has a small water cluster and is easy to drink, so that delicious food can be obtained even when used for rice or coffee.
【0030】また、汚水浄化処理においても前述したよ
うに、ゼオライト系水質浄化剤は多孔物質であって有害
物質を分解して吸着し、凝集させる特性を有しているた
め、いかなる汚水でも汚れを速やかに分離して綺麗に
し、また、水中の重金属類を吸着して溶出しないため産
業廃棄物にならなず再利用が可能であり、このゼオライ
ト系水質浄化剤を大量に使用してもpHの変動がないと
いう効果がある。しかも、製法が簡単であって、また、
安価に製造することができ、使用も簡単で容易であるな
どの優れた特徴を有している。In the sewage purification treatment, as described above, the zeolite-based water purification agent is a porous substance and has the property of decomposing, adsorbing, and coagulating harmful substances. It quickly separates and cleans, and because it does not adsorb and dissolve heavy metals in water, it can be reused without becoming industrial waste. There is an effect that there is no fluctuation. Moreover, the manufacturing method is simple,
It has excellent features such as being inexpensive to manufacture and easy and easy to use.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 1/68 510 C02F 1/68 510Z 520 520N 520D 520M 530 530A 540 540A 540Z ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI C02F 1/68 510 C02F 1/68 510Z 520 520N 520D 520M 530 530A 540 540A 540Z
Claims (8)
粒化したあらゆる多孔物質と二水石膏と可溶性無水石膏
との粉末混合物とを添加混合して成り、水に含有されて
いる汚水及び有機物質を除去し、水中にミネラル成分を
溶出することにより水のクラスターがより小さい状態で
得られることを特徴とするゼオライト系水質浄化剤。1. Sewage and organic substances contained in water, comprising powder zeolite as a main component, and adding and mixing all the finely divided porous substances and a powder mixture of gypsum dihydrate and soluble anhydrite. A zeolite-based water purification agent characterized in that water is removed in a small state by removing water and elute mineral components into water.
種が貝化石であることを特徴とする請求項1記載のゼオ
ライト系水質浄化剤。2. The zeolite-based water purification agent according to claim 1, wherein the porous substance is harmless to humans and animals, and one of the substances is shell fossils.
し、300℃以下の温度で乾燥したこれらの粉砕物質6
0〜80重量%と、二水石膏と可溶性無水石膏とを水に
溶解し、これらの溶解物と、非晶質物質との粉末混合物
20〜40%重量%とを混合することにより得られるこ
とを特徴とするゼオライト系水質浄化剤。3. The pulverized zeolite and the porous material are pulverized and dried at a temperature of 300 ° C. or less.
0 to 80% by weight, obtained by dissolving gypsum and soluble anhydrite in water, and mixing these dissolved materials with 20 to 40% by weight of a powder mixture of an amorphous substance. A zeolite-based water purification agent characterized by the following.
種が貝化石であることを特徴とする請求項3記載のゼオ
ライト系水質浄化剤。4. The zeolite-based water purification agent according to claim 3, wherein the porous substance is harmless to humans and animals, and one of the substances is shell fossils.
とする請求項3又は4のいずれか一項に記載のゼオライ
ト系水質浄化剤。5. The zeolite-based water purifying agent according to claim 3, wherein the amorphous substance is water glass.
化力を有することを特徴とする請求項1から5のいずれ
か一項に記載のゼオライト系水質浄化剤。6. The zeolite-based water purification agent according to claim 1, wherein the zeolite-based water purification agent has a purifying power for sewage.
濁粒子を取込んだ後に急速凝集によって沈降させること
により得られることを特徴とするゼオライト系水質浄化
剤。7. A zeolite-based water purification agent comprising a mixture of a coagulation nucleus and a carrier, and obtained by taking suspended particles and then sedimenting by rapid coagulation.
による沈降剤であることを特徴とする請求項7に記載の
ゼオライト系水質浄化剤。8. The zeolite-based water purification agent according to claim 7, wherein the zeolite-based water-purification agent is a sedimentation agent by rapid coagulation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10391497A JPH10277541A (en) | 1997-04-07 | 1997-04-07 | Zeolite type water purifying agent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10391497A JPH10277541A (en) | 1997-04-07 | 1997-04-07 | Zeolite type water purifying agent |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10277541A true JPH10277541A (en) | 1998-10-20 |
Family
ID=14366703
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10391497A Pending JPH10277541A (en) | 1997-04-07 | 1997-04-07 | Zeolite type water purifying agent |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10277541A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002066312A (en) * | 2000-08-31 | 2002-03-05 | Mitsubishi Rayon Co Ltd | Adsorbent for water purifier and water purifier using the same |
| WO2005009610A1 (en) * | 2003-07-25 | 2005-02-03 | Japan Envirochemicals, Ltd. | Heavy metal ion adsorbing agent |
| WO2010103624A1 (en) * | 2009-03-11 | 2010-09-16 | 浦野 哲一 | System for water purification |
| JP2013000625A (en) * | 2011-06-14 | 2013-01-07 | Kikuchi Takahiro | Water purifying agent |
| JP2017000045A (en) * | 2015-06-08 | 2017-01-05 | ジェックス株式会社 | Aquarium sand |
| RU2685673C1 (en) * | 2018-08-07 | 2019-04-22 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Петербургский государственный университет путей сообщения Императора Александра I" | Method of sewage treatment from heavy metal ions |
| CN115321622A (en) * | 2022-08-24 | 2022-11-11 | 萍乡宝海锌营养科技有限公司 | Preparation method of mineral element composition |
| KR102604098B1 (en) * | 2023-08-23 | 2023-11-20 | 주식회사 다봄씨엔에스 | Water quality improvement composition containing zeolite and method for preparing the same |
-
1997
- 1997-04-07 JP JP10391497A patent/JPH10277541A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002066312A (en) * | 2000-08-31 | 2002-03-05 | Mitsubishi Rayon Co Ltd | Adsorbent for water purifier and water purifier using the same |
| WO2005009610A1 (en) * | 2003-07-25 | 2005-02-03 | Japan Envirochemicals, Ltd. | Heavy metal ion adsorbing agent |
| WO2010103624A1 (en) * | 2009-03-11 | 2010-09-16 | 浦野 哲一 | System for water purification |
| JP2013000625A (en) * | 2011-06-14 | 2013-01-07 | Kikuchi Takahiro | Water purifying agent |
| JP2017000045A (en) * | 2015-06-08 | 2017-01-05 | ジェックス株式会社 | Aquarium sand |
| RU2685673C1 (en) * | 2018-08-07 | 2019-04-22 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Петербургский государственный университет путей сообщения Императора Александра I" | Method of sewage treatment from heavy metal ions |
| CN115321622A (en) * | 2022-08-24 | 2022-11-11 | 萍乡宝海锌营养科技有限公司 | Preparation method of mineral element composition |
| KR102604098B1 (en) * | 2023-08-23 | 2023-11-20 | 주식회사 다봄씨엔에스 | Water quality improvement composition containing zeolite and method for preparing the same |
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