JP2002219489A - Method for removing and recovering phosphorus using microorganism - Google Patents
Method for removing and recovering phosphorus using microorganismInfo
- Publication number
- JP2002219489A JP2002219489A JP2001015665A JP2001015665A JP2002219489A JP 2002219489 A JP2002219489 A JP 2002219489A JP 2001015665 A JP2001015665 A JP 2001015665A JP 2001015665 A JP2001015665 A JP 2001015665A JP 2002219489 A JP2002219489 A JP 2002219489A
- Authority
- JP
- Japan
- Prior art keywords
- phosphorus
- mold
- accumulated
- aqueous solution
- conditions
- 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.)
- Withdrawn
Links
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title claims abstract description 134
- 229910052698 phosphorus Inorganic materials 0.000 title claims abstract description 134
- 239000011574 phosphorus Substances 0.000 title claims abstract description 134
- 238000000034 method Methods 0.000 title claims abstract description 28
- 244000005700 microbiome Species 0.000 title description 5
- 239000007787 solid Substances 0.000 claims abstract description 4
- 241000221961 Neurospora crassa Species 0.000 claims description 19
- 239000003795 chemical substances by application Substances 0.000 claims description 12
- 239000007864 aqueous solution Substances 0.000 claims description 11
- 238000011084 recovery Methods 0.000 claims description 7
- 241000228245 Aspergillus niger Species 0.000 claims description 5
- 241000351920 Aspergillus nidulans Species 0.000 claims description 4
- 150000001413 amino acids Chemical class 0.000 claims description 4
- 230000003100 immobilizing effect Effects 0.000 claims description 4
- 239000001888 Peptone Substances 0.000 claims description 3
- 108010080698 Peptones Proteins 0.000 claims description 3
- 235000019319 peptone Nutrition 0.000 claims description 3
- 235000000346 sugar Nutrition 0.000 claims description 3
- 150000008163 sugars Chemical class 0.000 claims description 3
- 241000221960 Neurospora Species 0.000 claims description 2
- 235000001014 amino acid Nutrition 0.000 claims description 2
- 150000007524 organic acids Chemical class 0.000 claims description 2
- 235000005985 organic acids Nutrition 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 229910019142 PO4 Inorganic materials 0.000 description 11
- 238000009825 accumulation Methods 0.000 description 11
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 11
- 239000010452 phosphate Substances 0.000 description 11
- 241000894006 Bacteria Species 0.000 description 10
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 10
- 239000002351 wastewater Substances 0.000 description 10
- 239000010802 sludge Substances 0.000 description 8
- 238000002425 crystallisation Methods 0.000 description 7
- 230000008025 crystallization Effects 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 5
- 241000588624 Acinetobacter calcoaceticus Species 0.000 description 4
- 230000015271 coagulation Effects 0.000 description 4
- 238000005345 coagulation Methods 0.000 description 4
- 102220201851 rs143406017 Human genes 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 3
- 235000019796 monopotassium phosphate Nutrition 0.000 description 3
- PJNZPQUBCPKICU-UHFFFAOYSA-N phosphoric acid;potassium Chemical compound [K].OP(O)(O)=O PJNZPQUBCPKICU-UHFFFAOYSA-N 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241001362614 Crassa Species 0.000 description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 229910052588 hydroxylapatite Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- XYJRXVWERLGGKC-UHFFFAOYSA-D pentacalcium;hydroxide;triphosphate Chemical compound [OH-].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O XYJRXVWERLGGKC-UHFFFAOYSA-D 0.000 description 2
- -1 polypropylene Polymers 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 241000589291 Acinetobacter Species 0.000 description 1
- 241000182988 Assa Species 0.000 description 1
- 241000206602 Eukaryota Species 0.000 description 1
- 229920000388 Polyphosphate Polymers 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 241000589516 Pseudomonas Species 0.000 description 1
- 241000589774 Pseudomonas sp. Species 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- CKMXBZGNNVIXHC-UHFFFAOYSA-L ammonium magnesium phosphate hexahydrate Chemical compound [NH4+].O.O.O.O.O.O.[Mg+2].[O-]P([O-])([O-])=O CKMXBZGNNVIXHC-UHFFFAOYSA-L 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 241000902900 cellular organisms Species 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- AIUDWMLXCFRVDR-UHFFFAOYSA-N dimethyl 2-(3-ethyl-3-methylpentyl)propanedioate Chemical class CCC(C)(CC)CCC(C(=O)OC)C(=O)OC AIUDWMLXCFRVDR-UHFFFAOYSA-N 0.000 description 1
- ZPWVASYFFYYZEW-UHFFFAOYSA-L dipotassium hydrogen phosphate Chemical compound [K+].[K+].OP([O-])([O-])=O ZPWVASYFFYYZEW-UHFFFAOYSA-L 0.000 description 1
- 229910000396 dipotassium phosphate Inorganic materials 0.000 description 1
- 235000019797 dipotassium phosphate Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229940066779 peptones Drugs 0.000 description 1
- 239000001205 polyphosphate Substances 0.000 description 1
- 235000011176 polyphosphates Nutrition 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229910052567 struvite Inorganic materials 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
Description
ãïŒïŒïŒïŒã[0001]
ãçºæã®å±ããæè¡åéãæ¬çºæã¯ããªã³èç©èœãæã
ãã«ããå©çšããŠããªã³ãé€å»ããã³ååããæ¹æ³ã«é¢
ãããã®ã§ããã[0001] The present invention relates to a method for removing and recovering phosphorus by utilizing a mold having a phosphorus accumulation ability.
ãïŒïŒïŒïŒã[0002]
ãåŸæ¥ã®æè¡ãææ°Žäžãããªã³ãé€å»ããããã«ãåçš®
éå±å¡©ãçšããåéæ²æ®¿æ³ãæ¶æè±ãªã³æ³ããããã¯å«
æ°ã»å¥œæ°æŽ»æ§æ±æ³¥æ³ãå©çšãããŠãããããããAlãF
eãCaå¡©ãçšããåéæ²æ®¿æ³ã¯è¬å€ã³ã¹ããé«ããå ã
ãŠãçæããæ²æ®¿ç©ã¯ç£æ¥å»æ£ç©ãšããŠåŠåãããŠãã
ããããã®åŠçè²»çšã倧ããªåé¡ãšãªã£ãŠããã2. Description of the Related Art In order to remove phosphorus from wastewater, a coagulation precipitation method using various metal salts, a crystallization phosphorus removal method, or an anaerobic / aerobic activated sludge method is used. But Al, F
e, The coagulation precipitation method using Ca salt has a high chemical cost, and in addition, the generated precipitate is disposed of as industrial waste.
ãïŒïŒïŒïŒãæ¶æè±ãªã³æ³ã®äžã€ãšããŠãããããã·ã«
ã¢ãã¿ã€ãã®ç𮿶ãçšããŠãªã³ãå¹çããããããã·ã«
ã¢ãã¿ã€ãã«å€æãããããé€å»ããæ¹æ³ãç¥ãããŠã
ãããããããã®æ¹æ³ã§ã¯çææ®¿ç©ã¯å°ãªããªããã®
ã®ãæ¶²äžã® HCO3 - ã€ãªã³ãæ¶æãé»å®³ãããããäžåºŠ
é
žæ§ã«ã㊠HCO3 - ãé€å»ããåŸã匱ã¢ã«ã«ãªåŽã«pHã
ãã©ãå¿
èŠãããããã®ãããåéæ²æ®¿æ³ãšåæ§ã«è¬å€
ã«ããã©ã³ãã³ã°ã³ã¹ãã倧ãããªãåé¡ãããããŸ
ããããäžã€ã®æ¶æè±ãªã³æ³ã§ããã¹ãã©ãã€ãæ¶ææ³
ã¯ãæ¯èŒçãªã³æ¿åºŠãé«ãææ°Žã§ããã°é©çšã§ãããã
äœæ¿åºŠã®ãªã³ææ°Žã§ã¯ããã®æ¶æå¹çãäœäžããã[0003] As one of the crystallization dephosphorization methods, there is known a method of efficiently converting phosphorus to hydroxylapatite using a seed crystal of hydroxylapatite and removing it. However, although the product gluteal was reduced in this way, HCO 3 in the liquid - for ions to inhibit crystallization, HCO 3 and once acidic - After removal, it is necessary to return the pH to a weakly alkaline side . For this reason, there is a problem that the running cost due to the chemical becomes large similarly to the coagulation sedimentation method. In addition, struvite crystallization, which is another crystallization dephosphorization method, can be applied to wastewater having a relatively high phosphorus concentration,
With low-concentration phosphorus drainage, the crystallization efficiency is reduced.
ãïŒïŒïŒïŒãäžæ¹å«æ°ã»å¥œæ°æŽ»æ§æ±æ³¥æ³ã¯ãçç©ã®æã€
ãªã³èç©èœãå©çšããŠãªã³ãé€å»ããæ¹æ³ã§ããããã©
ã³ãã³ã°ã³ã¹ãã¯äœããã®ã®ãçç©çžã®å¶åŸ¡ãé£ããã
ãªã³é€å»ãäžå®å®ã§ããããšã倧ããªåé¡ãšãªã£ãŠã
ãã[0004] On the other hand, the anaerobic / aerobic activated sludge method is a method of removing phosphorus by utilizing the phosphorus accumulation ability of living organisms. However, although running costs are low, it is difficult to control the biota.
An unstable phosphorus removal is a major problem.
ãïŒïŒïŒïŒã以äžã®ããã«ãéå±å¡©ãå©çšããåéæ²æ®¿
æ³ã§ã¯ã©ã³ãã³ã°ã³ã¹ãã®é¢ã§ã®åé¡ãããããŸã嫿°
ã»å¥œæ°æŽ»æ§æ±æ³¥æ³ã§ã¯åŠçã®å®å®æ§ã®é¢ã§å€§ããªåé¡ã
æ®ã£ãŠãããAs described above, the coagulation sedimentation method using a metal salt has a problem in running cost, and the anaerobic / aerobic activated sludge method has a large problem in treatment stability.
ãïŒïŒïŒïŒã[0006]
ãçºæã解決ããããšãã課é¡ãæ¬çºæã¯äžèšäºæ
ã«é
ã¿ãŠãªããããã®ã§ããããã®èª²é¡ã¯ãçµæžçãã€å®å®
ãªãªã³é€å»æè¡ãéçºããããšã§ãããSUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and an object thereof is to develop an economical and stable phosphorus removal technique.
ãïŒïŒïŒïŒã[0007]
ã課é¡ã解決ããããã®ææ®µãæ¬çºæè
ã¯ãåŸæ¥ããã
éºäŒåŠã®åéçã§ç ç©¶ææãšããŠçšããããŠããã«ãã
é«ããªã³èç©èœãæã€ããšãèŠåºãããã®ãªã³èç©èœã
æããã«ããå©çšããããšã«ãããªã³ãé€å»ããæè¡ã
宿ããã«è³ã£ããæŽã«ããããã«ãã®ãã¡ç¹ã«Neuros
pora crassaã¯ãå¥œæ°æ§æ¡ä»¶äžã§ã¯ãªã³ãåã蟌ãã§è
ç©ããäžæ¹ã嫿°æ¡ä»¶äžã§ã¯èç©ãããªã³ãæŸåºããèœ
åãæããããšãèŠåºãããã®ã«ããå©çšããããšã«ã
ãããªã³ãååããæè¡ã宿ããã«è³ã£ããå ããŠã
ã«ãã¯è糞ã䌞ã°ãããšã«ãã£ãŠçè²ããæ§è³ªãæã€ã
ãšãããé©åœãªæ
äœãçšããããšã«ãã£ãŠå®¹æã«åºå®å
ã§ããããšã«åºã¥ããèäœå¯åºŠã®é«ããªã³ã®é€å»å€ãã
ã³ååå€ã宿ããã«è³ã£ããMeans for Solving the Problems The present inventor has conventionally proposed:
The present inventors have found that mold used as a research material in the field of genetics has a high phosphorus accumulation ability, and have completed a technique for removing phosphorus by using mold having the phosphorus accumulation ability. Furthermore, among these molds, especially Neuros
pora crassa has the ability to take up and accumulate phosphorus under aerobic conditions, but has the ability to release the accumulated phosphorus under anaerobic conditions, and complete the technology to recover phosphorus by utilizing this mold Reached. in addition,
Since mold has the property of growing by elongating mycelia, it can be easily immobilized by using an appropriate carrier, and thus a phosphorus removing agent and a collecting agent having a high cell density have been completed.
ãïŒïŒïŒïŒãå³ã¡ãæ¬çºæã®èª²é¡ã¯ãäžèšã®ïŒïŒïŒã
ïŒïŒïŒã«ãã£ãŠéæããããThat is, the objects of the present invention are as follows:
This is achieved by (6).
ãïŒïŒïŒïŒãïŒïŒïŒãªã³ãåã蟌ãã§èç©ããèœåãæ
ããã«ãããåºçžæ
äœã«åºå®åããŠãªããªã³é€å»å€ã§ã
ãã(1) A phosphorus-removing agent obtained by immobilizing a mold capable of taking up and accumulating phosphorus on a solid-phase carrier.
ãïŒïŒïŒïŒãïŒïŒïŒåèšã«ãããAspergillus nigerãA
spergillus nigerãNeurospora crassaãNeurospora cr
assaãããã³Emericella nidulansãããªã矀ããéžæ
ããã ïŒïŒïŒå¥œæ°æ¡ä»¶ã§ã¯ãªã³ãåã蟌ãã§èç©ãã嫿°æ¡ä»¶
äžã§ã¯èç©ãããªã³ãæŸåºããèœåãæããã«ãããåº
çžæ
äœã«åºå®åããŠãªããªã³ååå€ã(2) The mold is Aspergillus niger, A
spergillus niger, Neurospora crassa, Neurospora cr
selected from the group consisting of assa and Emericella nidulans (3) A mold capable of taking up and accumulating phosphorus under aerobic conditions and releasing accumulated phosphorus under anaerobic conditions is immobilized on a solid support. Phosphorus recovery agent.
ãïŒïŒïŒïŒãïŒïŒïŒåèšã«ãããNeurospora crassaã§
ããè«æ±é
ïŒã«èšèŒã®ãªã³ã®ååé€å»å€ã(4) The agent for recovering and removing phosphorus according to claim 3, wherein the mold is Neurospora crassa.
ãïŒïŒïŒïŒãïŒïŒïŒè«æ±é
ïŒãŸãã¯ïŒã«èšèŒã®ãªã³é€å»
å€ã«ãªã³å«ææ°Žæº¶æ¶²ãæ¥è§Šãããããšã«ãããåèšã«ã
ã«ãªã³ãåã蟌ãŸããŠèç©ãããããšãç¹åŸŽãšãããªã³
å«ææ°Žæº¶æ¶²äžã®ãªã³é€å»æ¹æ³ã(5) A method for removing phosphorus from a phosphorus-containing aqueous solution, wherein the mold is taken up and accumulated by contacting the phosphorus-containing aqueous solution with the phosphorus-removing agent according to claim 1 or 2. .
ãïŒïŒïŒïŒãïŒïŒïŒè«æ±é
ïŒãŸãã¯ïŒã«èšèŒã®ãªã³åå
å€ãšãªã³å«ææ°Žæº¶æ¶²ãšãå¥œæ°æ¡ä»¶äžã§æ¥è§Šãããããšã«
ãããåèšã«ãã«ãªã³ãåã蟌ãŸããŠèç©ãããåŸãã
ãã嫿°æ¡ä»¶äžã§ä¿æããããšã«ããåèšã«ãã«èç©ã
ãããªã³ãæŸåºãããããšãç¹åŸŽãšãããªã³å«ææ°Žæº¶æ¶²
äžã®ãªã³é€å»æ¹æ³ã(6) By contacting the phosphorus-recovering agent according to claim 3 with an aqueous solution containing phosphorus under aerobic conditions, phosphorus is taken in and accumulated in the mold, and is then subjected to anaerobic conditions. A method for removing phosphorus from a phosphorus-containing aqueous solution, wherein the phosphorus accumulated in the mold is released by holding the phosphorus under the mold.
ãïŒïŒïŒïŒãïŒïŒïŒåèšã«ãã嫿°æ¡ä»¶äžã§ä¿æããé
ã«ãç³ãææ©é
žé¡ããããã³ãã¢ããé
žé¡çãååšãã
ãããšãç¹åŸŽãšããè«æ±é
ïŒã«èšèŒã®ãªã³ã®ååæ¹æ³ã(7) The method for recovering phosphorus according to claim 6, wherein sugars, organic acids, peptones, amino acids and the like are present when the mold is kept under anaerobic conditions.
ãïŒïŒïŒïŒã[0015]
ã宿œã®æ æ§ã以äžãæ¬çºæãããå ·äœçã«è©³è¿°ãããDESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in more detail.
ãïŒïŒïŒïŒãæ¬çºæã«çšããã«ããšããŠã¯ããªã³èç©èœ
ãæããã«ãã§ããã°ç¹ã«éå®ãããªãããAspergillu
s nigerãAspergillus nigerãNeurospora crassaãEme
ricella nidulansçãæããããšãã§ããããã®ãã¡ã
ç¹ã«å¥œãŸããã®ã¯Neurosporacrassaã§ããããããã®è
æ ªã¯ãæ¬çºæäžã«æŒããŠããªã³èç©èã§ããPseudomona
s sp. Acinetobacter calcoaceticus ãšåçã®ãªã³èç©
èœåãæã€ããšã確èªãããŠãããThe mold used in the present invention is not particularly limited as long as it has a phosphorus accumulation ability.
s niger, Aspergillus niger, Neurospora crassa, Eme
ricella nidulans and the like. this house,
Particularly preferred is Neurosporacrassa. These strains are referred to in the present invention as Pseudomona, a phosphorus-accumulating bacterium.
It has been confirmed that it has the same phosphorus accumulation ability as s sp. Acinetobacter calcoaceticus.
ãïŒïŒïŒïŒãæŽã«ãç¹ã«å¥œãŸããã«ãã§ããNeurospora
crassaã¯ãå¥œæ°æ§æ¡ä»¶äžã§ã¯ãªã³ãåã蟌ãã§èç©ã
ãäžæ¹ã嫿°æ¡ä»¶äžã§ã¯èç©ãããªã³ãæŸåºããèœåã
æãããåŸã£ãŠãNeurospora crassaãå©çšããã°ãæ
æ°Žçããåã«ãªã³ãé€å»ããã ãã§ãªããé€å»ãããªã³
ã容æã«ååããããšãå¯èœã§ãããFurthermore, a particularly preferred mold, Neurospora
Crassa has the ability to take up and accumulate phosphorus under aerobic conditions, while releasing accumulated phosphorus under anaerobic conditions. Therefore, if Neurospora crassa is used, it is possible not only to remove phosphorus from wastewater and the like, but also to easily recover the removed phosphorus.
ãïŒïŒïŒïŒãçç©ã«ãªã³ãèç©ããææ°Žäžã®ãªã³ãé€å»
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äœãçšããããšã«ãã容æã«
åºå®åãå¯èœã§ãããèäœå¯åºŠã®é«ããªã³é€å»èšåã®æ§
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ããææã§ããã°ãç¹ã«å¶éãããããšãªã䜿çšããã
ãšãã§ãããWhen phosphorus is accumulated in organisms and phosphorus in wastewater is removed, it is necessary not only that the organisms have a high phosphorus accumulation ability, but also that the cell density is kept high. Since mold has the property of growing by elongating mycelium, it can be easily immobilized by using an appropriate carrier, and a phosphorus removal facility having a high cell density can be constructed. In that case, as the solid phase carrier used for immobilizing the above-mentioned mold, any porous material having a water retention property and having a gap through which the mold hypha can be extended and serves as an air passage can be used. . As the material, a resin such as polypropylene, ceramics, or any other material that can be processed so as to satisfy the above-described properties as a carrier can be used without any particular limitation.
ãïŒïŒïŒïŒãæ¬çºæã®æ¹æ³ã«ããåŠçãã¹ã察象ã§ãã
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ãåŠçããå Žåã«æ¯èŒããŠãªã³æ¿åºŠãé«ããªã£ãŠããã
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èœãšãªããExamples of the phosphorus-containing aqueous solution to be treated by the method of the present invention include phosphorus-containing wastewater and secondary treatment water with residual phosphorus. When phosphorus is recovered in an aqueous solution by applying the present invention, it can be used as a liquid fertilizer. In some cases, phosphorus can be precipitated and recovered by applying a crystallization dephosphorization method. In this case, since the phosphorus concentration is higher than in the case where the phosphorus-containing wastewater is directly treated by a chemical technique, the recovery rate can be improved by increasing the efficiency of crystal precipitation.
ãïŒïŒïŒïŒãæ¬çºæã«ãããŠNeurospora crassaãå©çš
ããŠãªã³ãååããå Žåãå
ããªã³å«ææ°Žæº¶æ¶²äžã«å¥œæ°
æ¡ä»¶ãç¶æããŠãNeurospora crassaã«ãªã³ãåã蟌ãŸ
ããŠèç©ãããããã®ãããªå¥œæ°æ¡ä»¶ãç¶æãããã
ã«ãå¿
èŠã§ããã°ç©ºæ°ã溶液äžã«ãããªã³ã°ããŠãã
ãããªã³ãåã蟌ãŸããŠèç©ãããããæ¬¡ã«ã溶液ãå«
æ°æ¡ä»¶ã«ç¶æããŠãNeurospora crassaã«èç©ããããª
ã³ãæŸåºãããããã®å«æ°æ¡ä»¶ãç¶æããææ®µãšããŠ
ã¯ãçªçŽ ã¬ã¹çã®äžæŽ»æ§ã¬ã¹ã溶液äžã«ãããªã³ã°ãã
ãªã©ã®ææ®µãçšããããšãã§ãããIn the present invention, when recovering phosphorus using Neurospora crassa, first, aerobic conditions are maintained in a phosphorus-containing aqueous solution, and phosphorus is taken up and accumulated in Neurospora crassa. To maintain such aerobic conditions, air may be bubbled through the solution if necessary. Once phosphorus is incorporated and accumulated, the solution is then maintained under anaerobic conditions to release the accumulated phosphorus in Neurospora crassa. As means for maintaining the anaerobic condition, means such as bubbling an inert gas such as nitrogen gas into the solution can be used.
ãïŒïŒïŒïŒããªãã嫿°æ¡ä»¶äžã§ã®ãªã³æŸåºã¯ãåã«å
å¿æ§œå
ã嫿°æ¡ä»¶ã«ããã ãã§ãå¯èœã§ããããæŸåºé
床ãäžããããã«ã¯ãã°ã«ã³ãŒã¹ãªã©ã®ç³ããããã³ãª
ã©ã®ã¢ããé
žé¡ããã®ä»ã®ææ©ç©ã®æ·»å ããã广çã§
ãããåŸã£ãŠã嫿°æ¡ä»¶äžã§ã®ãªã³æŸåºæ®µéã§ã¯ãäžèš
ç©è³ªãåç¬ã§ãããã¯æ··åããŠæ·»å ããããšãæãŸã
ãããããã®ææ©ç©ã¯ãå¥œæ°æ¡ä»¶äžã«ããããªã³ã®åã
蟌ã¿ãããªãã¡èäœå
ã«ããããªã³é
žããã®ããªãªã³é
ž
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èŠãªçç©åŠçãšãã«ã®ãŒæºãšããªãã®ã§ããªã³
æŸåºãä¿é²ããã®ã¿ãªãããå¥œæ°æ¡ä»¶äžã§ã®ãªã³åã蟌
ã¿ããä¿é²ãããšèããããã[0021] Phosphorus release under anaerobic conditions can be achieved simply by subjecting the reaction tank to anaerobic conditions. However, in order to increase the release rate, sugars such as glucose, amino acids such as peptone, and other amino acids. Is more effective. Therefore, in the phosphorus release step under anaerobic conditions, it is desirable to add the above substances alone or as a mixture. Since these organic substances serve as a biological energy source necessary for the uptake of phosphorus under aerobic conditions, that is, the synthesis of polyphosphate from phosphoric acid in cells, they not only promote phosphorus release but also under aerobic conditions. May also promote phosphorus uptake at
ãïŒïŒïŒïŒã以äžã®ããã«ãªã³å«æææ°Žãå¥œæ°æ¡ä»¶äžã§
åŠçããŠãªã³ãé€å»ãããªã³é€å»çãäœäžããããæ¬¡ã«
嫿°æ¡ä»¶ãšããŠãªã³é
žãæŸåºãããããªã³é
žãæŸåºãã
èäœã¯ãå¥œæ°æ¡ä»¶äžã«ããããªã³é
žåã蟌ã¿èœãå埩ã
ããããç¹°ãè¿ããªã³é€å»ãè¡ãããããšãã§ããããŸ
ãé£ç¶çã«æµåºããææ°Žã«ã¯æ¬è£
眮ãïŒåŒçšæãã亀äº
ã«é転ããããšã«ãã£ãŠå¯Ÿå¿å¯èœãšãªããAs described above, the phosphorus-containing wastewater is treated under aerobic conditions to remove phosphorus, and when the phosphorus removal rate decreases, phosphoric acid is then released under anaerobic conditions. Since the cells that have released phosphate restore their ability to take up phosphate under aerobic conditions, phosphorus can be removed repeatedly. It is possible to cope with the continuous drainage by preparing two sets of this device and operating them alternately.
ãïŒïŒïŒïŒã以äžãæ¬çºæã宿œäŸã«ãã説æãããã
æ¬çºæã®æè¡çç¯å²ã¯ããã宿œäŸã«ããäœãå¶éãã
ããã®ã§ã¯ãªããHereinafter, the present invention will be described with reference to Examples.
The technical scope of the present invention is not limited by these examples.
ãïŒïŒïŒïŒã[0024]
ã宿œäŸã宿œäŸïŒ 埮çç©ãçšããŠææ°Žã«å«ãŸãããªã³ã®é€å»ãåã³ååã
è¡ãå Žåãçšãã埮çç©ã®ãªã³ã®èç©éãå€ãå¿
èŠãã
ãããããŸã§ã«Acinetobactorå±ãArthrobactorå±ãPse
udomonaså±çã®åŸ®çç©ããªã³èç©éã®å€ããã¯ããªã¢ãš
ããŠåé¢ãããŠãããæã
ã¯çæ žçç©ã§ããã«ãé¡ãã
ãã®çްèã®å€§ãããããªã³ã®åã蟌ã¿ãèç©èœåã®ãã
ã³ã·ã£ã«ãããããšãè²§æ 逿¡ä»¶ã§ãçè²ã§ãããšãã
çæŽ»ç°ã®ç¹æ§çã«çç®ãããªã³é€å»ã·ã¹ãã ã«é©çšã§ã
ãã®ã§ã¯ãªãããšèãããããã§ãã«ãé¡ã®ãªã³èç©é
ã«é¢ããŠãäžèšã«ç€ºãããã¯ããªã¢ãšãæ¯èŒãããæ¯èŒ
ãããã¯ããªã¢ã¯ããªã³èç©èã§ããAcinetobacter ca
lcoaceticusãPseudomonas sp.ã§ãããEXAMPLE 1 When removing and recovering phosphorus contained in wastewater using microorganisms, it is necessary that the amount of accumulated phosphorus of the microorganisms used is large. Acinetobactor, Arthrobactor, Pse
Microorganisms such as genus udomonas have been isolated as bacteria with high phosphorus accumulation. We know that eukaryotes, molds,
Focusing on the potential of phosphorus uptake and accumulation ability based on the size of the cells, and the characteristics of the life cycle that can grow under oligotrophic conditions, etc., we thought that it could be applied to a phosphorus removal system. Thus, the amount of phosphorus accumulated in molds was compared with the bacteria shown above. The bacteria compared were Acinetobacter ca, a phosphorus-accumulating bacterium.
lcoaceticus, Pseudomonas sp.
ãïŒïŒïŒïŒã衚ïŒã«ç€ºããæ¹å€Czapek's Doxå¹å°ã«ãªã³
é
žæ¿åºŠãšããŠ60 mg/Lãšãªãããã«ãªã³é
žæ°ŽçŽ ã«ãªãŠã
ãæ·»å ããå¹å°ã§ã衚ïŒã«ç€ºã埮çç©ãå¹é€ãããå¹é€
ãå§ããŠ24æéåŸãããããã®å¹é€æ¶²ããèäœãåå
ãããã®èäœééãæž¬å®ããããŸããå¹é€éå§æãåã³
å¹é€çµäºæã®å¹å°äžã®å
šãªã³æ¿åºŠã枬å®ãããã®å·®åé
ãèäœå
ã«åã蟌ãŸããå
šãªã³ãšãããThe microorganisms shown in Table 1 were cultured in a medium in which potassium hydrogen phosphate was added to the modified Czapek's Dox medium shown in Table 2 so that the phosphoric acid concentration became 60 mg / L. Twenty-four hours after the start of the culture, the cells were collected from each culture solution, and the cell weight was measured. At the start of the culture and at the end of the culture, the total phosphorus concentration in the medium was measured, and the difference was defined as the total phosphorus taken into the cells.
ãïŒïŒïŒïŒããã®çµæã衚ïŒã«ç€ºãããããã®çµæã
ããAspergillus nigerãAspergillusnigerãNeurospor
a crassaãEmericella nidulansã¯äœãããªã³ã®åã蟌
ã¿ããã³èç©èœåãæããããšãåãããç¹ã«ãN. cra
ssa(III)ïŒä»¥äžãN. crassaãšããïŒã¯ããªã³èç©ãã¯
ããªã¢ãšã»ãŒåçã®ãªã³èç©èœåãæã£ãŠãããšå€æã§
ããããŸãããããŸã§ã®æŽ»æ§æ±æ³¥ã«ãããªã³é€å»ã«é¢ã
ãç¥èŠããæ±æ³¥äžã®ãªã³ã®èç©éã¯ã2ã2.5 ïŒ
çšåºŠã«
ãšã©ãŸã£ãŠãããN. crassaã®ãªã³èç©èœåã¯ãããã
äžåããåŸã£ãŠãã«ãé¡äžã§æããªã³é
žèç©èœãé«ãN.
crassaæ ªã¯ããªã³é€å»ã»ååããã»ã¹ã«é©çšããããš
ãã§ãããTable 3 shows the results. From these results, Aspergillus niger, Aspergillusniger, Neurospor
It can be seen that both a crassa and Emericella nidulans have the ability to take up and accumulate phosphorus. In particular, N. cra
It can be determined that ssa (III) (hereinafter referred to as N. crassa) has a phosphorus storage ability substantially equal to that of phosphorus storage bacteria. In addition, from the knowledge of phosphorus removal by activated sludge, the accumulated amount of phosphorus in sludge is only about 2 to 2.5%, and the phosphorus accumulation capacity of N. crassa exceeds this. Therefore, N. has the highest phosphate accumulation ability among molds.
crassa strains can be applied to the phosphorus removal and recovery process.
ãïŒïŒïŒïŒã[0027]
ã衚ïŒã [Table 1]
ãïŒïŒïŒïŒã[0028]
ã衚ïŒã [Table 2]
ãïŒïŒïŒïŒã[0029]
ã衚ïŒã [Table 3]
ãïŒïŒïŒïŒã宿œäŸïŒ çç©åŠçã«ãªã³é€å»ãè¡ãå Žåã®æ¡ä»¶ãšããŠãçç©ã®ãª
ã³èç©èœåãé«ãããšãããããšãªããããªã³ã®åã蟌
ã¿é床ãé«ãããšãå¿
èŠã§ãããäŸãã°ãæ°Žæ»çæéã
çãåŠçããã»ã¹ã«é©çšãããšãããªã³èç©èœåã¯ãªã³
åã蟌ã¿é床ã«å¶éãããããããªã³åã蟌ã¿é床ã®é«
ãçç©ãçšããããšãæãŸãããããã§ã¯ã宿œäŸïŒãš
åæ§ã«ãæ¬çºæã§ããã«ãã®ãªã³åã蟌ã¿é床ãšããªã³
èç©ãã¯ããªã¢ã®ãããæ¯èŒãããExample 2 As conditions for biologically removing phosphorus, it is necessary that not only the ability of the organism to accumulate phosphorus be high, but also that the rate of phosphorus uptake be high. For example, when applied to a treatment process with a short water residence time, the ability to accumulate phosphorus is limited by the rate of phosphorus uptake, so it is desirable to use organisms with a high phosphorus uptake rate. Here, as in Example 1, the phosphorus uptake rate of the mold of the present invention was compared with that of the phosphorus-accumulating bacteria.
ãïŒïŒïŒïŒããªã³èç©èœåã®é«ãN. crassaãåã³å¯Ÿç
§
çç©ãšããŠãªã³èç©ãã¯ããªã¢ã§ããA. calcoaceticus
ããªã³é
žæ¿åºŠãšããŠã20 ÎŒMãšãªãããã«ãªã³é
žäºæ°ŽçŽ
ã«ãªãŠã ãå ããæ¹å€Czapek's Doxå¹å°ã«æ€èããå¹é€
ãããèäœãååããŠããªã³é
žåã蟌ã¿è©Šéšå¹å°ïŒççŽ
æºãå«ãŸãã30mg-PO4/Lãšãªãããã«ãªã³é
žäºæ°ŽçŽ ã«ãª
ãŠã ãå ããæ¹å€Czapek's Doxå¹å°ãpH7.0ïŒã§æŽæµ
ãããªã³é
žåã蟌ã¿è©Šéšå¹å°ã«èäœæ¿åºŠãã»ãŒ1g-dry_w
eight/lãšãªãããã«åæžæ¿ããå転æ¯ãšãããŠå¥œæ°æ¡
ä»¶ãšããåèæ ªã®ãªã³é
žåã蟌ã¿é床ã調ã¹ããN. crassa, which has a high phosphorus storage ability, and A. calcoaceticus, a phosphorus storage bacterium, as a control organism
Was inoculated into a modified Czapek's Dox medium supplemented with potassium dihydrogen phosphate at a phosphoric acid concentration of 20 ÎŒM, and cultured. The cells were collected and washed with a phosphate uptake test medium (modified Czapek's Dox medium, pH 7.0, containing no carbon source and containing potassium dihydrogen phosphate at 30 mg-PO 4 / L), Almost 1 g-dry_w in the phosphate uptake test medium
The suspension was resuspended to eight / l, and the suspension was shaken under aerobic conditions to examine the phosphate uptake rate of each strain.
ãïŒïŒïŒïŒã詊éšéå§åŸ30åéã®éã«ãèäœ1 gåœãã
åã蟌ãã ãªã³ééããç®åºããåèæ ªã®ãªã³é
žåã蟌
ã¿é床ã衚ããã°ã©ããå³ïŒã«ç€ºãããã®çµæãããN.
crassaã¯ããªã³èç©ãã¯ããªã¢ã§ããA. calcoaceticu
sãšåçã®ãªã³é
žåã蟌ã¿é床ãæã£ãŠãããN. crassa
æ ªã¯ããªã³é€å»ã»ååããã»ã¹ã«é©çšããããšãå¯èœã§
ãããšå€æã§ãããFIG. 1 is a graph showing the rate of phosphate uptake of each strain calculated from the weight of phosphorus taken up per gram of cells during 30 minutes after the start of the test. From this result, N.
crassa is a phosphorus-accumulating bacterium, A. calcoaceticu
s has the same phosphate uptake rate as N. crassa
The strain can be determined to be applicable to the phosphorus removal and recovery process.
ãïŒïŒïŒïŒã宿œäŸïŒ ãªã³èç©èœåã®é«ãN. crassaãåã³å¯Ÿç
§çç©ãšããŠãª
ã³èç©ãã¯ããªã¢ã§ããA. calcoaceticusããªã³é
žæ¿åºŠ
ãšããŠã20 ÎŒMãšãªãããã«ãªã³é
žäºæ°ŽçŽ ã«ãªãŠã ãå
ããæ¹å€Czapek's Doxå¹å°ã«æ€èããå¹é€ãããèäœã
ååããŠããªã³é
žåã蟌ã¿è©Šéšå¹å°ã§æŽæµãããªã³é
žå
ã蟌ã¿è©Šéšå¹å°ã«èäœæ¿åºŠãã»ãŒ1g-dry_weight/lãšãª
ãããã«åæžæ¿ããã宿œäŸïŒãšåæ§ã«ã奜æ°çã«ãªã³
ãåã蟌ãŸãããïŒæéçµéåŸã詊éšå¹å°ã«çªçŽ ã¬ã¹ã
å¹ã蟌ã¿ã匷å¶çã«å¹å°å
ã嫿°æ¡ä»¶ã«ãããšããã奜
æ°æ¡ä»¶äžã§åã蟌ãŸãããªã³ãåæŸåºãããããšãæã
ãã«ãªã£ãããã®çµæãå³ïŒã®ã°ã©ãå³ã«ç€ºããExample 3 Modified Czapek's Dox prepared by adding potassium dihydrogen phosphate to N. crassa having a high phosphorus accumulating ability and A. calcoaceticus, which is a phosphorus accumulating bacterium as a control organism, at a phosphoric acid concentration of 20 ÎŒM. The medium was inoculated and cultured. The cells were collected, washed with a phosphate uptake test medium, and resuspended in the phosphate uptake test medium so that the cell concentration was approximately 1 g-dry_weight / l. As in Example 2, phosphorus was aerobically incorporated. After a lapse of 3 hours, nitrogen gas was blown into the test medium to forcibly set the medium in an anaerobic condition. As a result, it was found that phosphorus taken in under the aerobic condition was released again. The results are shown in the graph of FIG.
ãïŒïŒïŒïŒããŸããåæ§ã®å®éšç³»ã§ã嫿°æ¡ä»¶ã«åãæ¿
ãããšãã«ã詊éšå¹å°ã«ææ©ç©ãé©å®ïŒæ¬å®æœäŸã§ã¯ã
ææ©ç©ãšããŠ100mg-TOC/Lçžåœã®ã°ã«ã³ãŒã¹ïŒå ããŠã
ãªã³ã®åæŸåºãããããšãããå ããªãç³»ãšæ¯èŒããŠã
æŸåºéåºŠãæ¿åºŠãé«ããªãããšãããã£ãïŒå³ïŒïŒããª
ããTOCïŒtotal organic carbonïŒã¯å
šææ©ççŽ éã衚
ããIn the same experimental system, when switching to anaerobic conditions, an organic substance is appropriately added to the test medium (in this example,
100 mg-TOC / L of glucose as organic matter)
When the phosphorus was released again,
It was found that the release rate and concentration increased (FIG. 3). In addition, TOC (total organic carbon) represents the total amount of organic carbon.
ãïŒïŒïŒïŒã以äžã®çµæãããã«ãN. crassaãçšãã
ãªã³å«æææ°Žäžã®ãªã³ãå¥œæ°æ¡ä»¶äžã§èäœå
ã«åã蟌ãŸ
ããããšã«ãããªã³é€å»ãè¡ããèäœå
ã«èç©ãããªã³
ã嫿°æ¡ä»¶äžã§åæŸåºãããããšã«ãã£ãŠãçç©åŠçãª
ã³é€å»ååã·ã¹ãã ãæ§ç¯ããããšãã§ãããFrom the above results, using mold N. crassa,
Builds a biological phosphorus removal and recovery system by removing phosphorus by incorporating phosphorus in phosphorus-containing wastewater into cells under aerobic conditions and releasing the phosphorus accumulated in the cells under anaerobic conditions can do.
ãïŒïŒïŒïŒã[0036]
ãçºæã®å¹æãæ¬çºæã«ããã°ãè¬å€çã®ã©ã³ãã³ã°ã³
ã¹ããå¿
èŠæå°éã«æŒããããããå®å®ãããªã³é€å»æ
è¡ãæäŸãããç¡æ©ç³»ãªã³å«æææ°ŽããåŸæ¥ã®æŽ»æ§æ±æ³¥
åŠççã®ïŒæ¬¡åŠçæ°Žããå¹ççã«ãªã³ãé€å»ããããšã
ã§ããããŸãããããŸã§é€å»ããã®ã¿ã§ååãå°é£ã§ã
ã£ããªã³ãååããããšãã§ãããAccording to the present invention, the running cost of chemicals and the like is kept to a minimum and a stable phosphorus removal technique is provided. The secondary treatment such as inorganic phosphorus-containing wastewater and conventional activated sludge treatment is provided. Phosphorus can be efficiently removed from water. In addition, it is possible to recover phosphorus, which has been difficult to recover only by removal.
ãïŒïŒïŒïŒããªããçç©åŠçãªãªã³é€å»èœåã¯ãªã³é€å»
æ§œã®çç©æ¿åºŠã«äŸåããããåŸæ¥ã®æŽ»æ§æ±æ³¥ãçšãããª
ã³é€å»ã®å Žåãé«ãçç©æ¿åºŠãç¶æããããšãå°é£ã§ã
ãããããªã³é€å»èœåã¯æŽ»æ§æ±æ³¥æ¿åºŠã«å¶éãããŠã
ããæ¬çºæã§ã¯ãã«ããè糞ãã®ã°ãããšã«ãã£ãŠçè²
ããæ§è³ªãå©çšããŠé©åœãªæ
äœã«åºå®åãããããèäœ
å¯åºŠã®é«ããªã³é€å»èšåãæ§ç¯ã§ããç¹åŸŽããããAlthough the biological phosphorus removal ability depends on the biological concentration in the phosphorus removal tank, it is difficult to maintain a high biological concentration in conventional phosphorus removal using activated sludge. Removal capacity was limited to the activated sludge concentration. In the present invention, the mold is immobilized on an appropriate carrier by utilizing the property of growing by growing the hypha, and therefore, there is a feature that a phosphorus removing facility having a high cell density can be constructed.
ãå³ïŒãåèæ ªã®ãªã³é žåã蟌ã¿é床ã瀺ãã°ã©ããFIG. 1 is a graph showing the phosphate uptake rate of each strain.
ãå³ïŒããªã³ã®åã蟌ã¿ã»åæŸåºå®éšãè¡ã£ãçµæã瀺
ãã°ã©ããFIG. 2 is a graph showing the results of a phosphorus uptake / rerelease experiment.
ãå³ïŒããªã³ã®åã蟌ã¿ã»åæŸåºã«äžããææ©ç©æ·»å ã®
广ã瀺ãã°ã©ããFIG. 3 is a graph showing the effect of adding an organic substance on phosphorus uptake and re-release.
âââââââââââââââââââââââââââââââââââââââââââââââââââââ ããã³ãããŒãžã®ç¶ã (51)Int.Cl.7 èå¥èšå·  ããŒãã³ãŒãã(åèïŒ //(ïŒïŒïŒ® 1/14 (ïŒïŒïŒ® 1/14  ïŒïŒïŒ² 1:645ïŒ ïŒ£ïŒïŒïŒ² 1:645ïŒ (ïŒïŒïŒ® 1/14 (ïŒïŒïŒ® 1/14  ïŒïŒïŒ² 1:645ïŒ ïŒ£ïŒïŒïŒ² 1:645ïŒ ââââââââââââââââââââââââââââââââââââââââââââââââââç¶ ã Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ã (Reference) // (C12N 1/14 (C12N 1/14 B C12R 1: 645) C12R 1: 645) (C12N 1 / 14 (C12N 1 / 14Z C12R 1: 645) C12R 1: 645)
Claims (7)
ã«ãããåºçžæ äœã«åºå®åããŠãªããªã³é€å»å€ã1. A phosphorus removing agent obtained by immobilizing a mold capable of taking up and accumulating phosphorus on a solid support.
gillus nigerãNeurospora crassaãNeurospora crass
aãããã³Emericella nidulansãããªã矀ããéžæãã
ã2. The method according to claim 1, wherein the mold is Aspergillus niger, Asper.
gillus niger, Neurospora crassa, Neurospora crass
a, and selected from the group consisting of Emericella nidulans
嫿°æ¡ä»¶äžã§ã¯èç©ãããªã³ãæŸåºããèœåãæããã«
ãããåºçžæ äœã«åºå®åããŠãªããªã³ååå€ã3. In aerobic conditions, phosphorus is taken up and accumulated,
A phosphorus recovery agent obtained by immobilizing a mold capable of releasing accumulated phosphorus under anaerobic conditions on a solid support.
è«æ±é ïŒã«èšèŒã®ãªã³ã®ååé€å»å€ã4. The agent for recovering and removing phosphorus according to claim 3, wherein the mold is Neurospora crassa.
ãªã³å«ææ°Žæº¶æ¶²ãæ¥è§Šãããããšã«ãããåèšã«ãã«ãª
ã³ãåã蟌ãŸããŠèç©ãããããšãç¹åŸŽãšãããªã³å«æ
氎溶液äžã®ãªã³é€å»æ¹æ³ã5. A method for removing phosphorus from a phosphorus-containing aqueous solution, comprising bringing a mold into which phosphorus is incorporated by accumulating the phosphorus-containing aqueous solution with the phosphorus-removing agent according to claim 1 or 2.
ãªã³å«ææ°Žæº¶æ¶²ãšãå¥œæ°æ¡ä»¶äžã§æ¥è§Šãããããšã«ã
ããåèšã«ãã«ãªã³ãåã蟌ãŸããŠèç©ãããåŸããã
ã嫿°æ¡ä»¶äžã§ä¿æããããšã«ããåèšã«ãã«èç©ãã
ããªã³ãæŸåºãããããšãç¹åŸŽãšãããªã³å«ææ°Žæº¶æ¶²äž
ã®ãªã³ååæ¹æ³ã6. A method in which phosphorus is taken in and accumulated in the mold by contacting the phosphorus recovery agent according to claim 3 with an aqueous solution containing phosphorus under aerobic conditions, and then the anaerobic condition is applied. Discharging the phosphorus accumulated in the mold by holding the phosphorus in the aqueous solution containing phosphorus.
ç³ãææ©é žé¡ããããã³ãã¢ããé žé¡çãååšãããã
ãšãç¹åŸŽãšããè«æ±é ïŒã«èšèŒã®ãªã³ã®ååæ¹æ³ã7. When the mold is kept under anaerobic conditions,
The method for recovering phosphorus according to claim 6, wherein sugars, organic acids, peptone, amino acids and the like are present.
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