JPH01266835A - Biological deodorizing method - Google Patents
Biological deodorizing methodInfo
- Publication number
- JPH01266835A JPH01266835A JP63091598A JP9159888A JPH01266835A JP H01266835 A JPH01266835 A JP H01266835A JP 63091598 A JP63091598 A JP 63091598A JP 9159888 A JP9159888 A JP 9159888A JP H01266835 A JPH01266835 A JP H01266835A
- Authority
- JP
- Japan
- Prior art keywords
- carrier
- microorganisms
- exhaust gas
- coated
- tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims description 12
- 230000001877 deodorizing effect Effects 0.000 title claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 244000005700 microbiome Species 0.000 claims abstract description 15
- 229920000642 polymer Polymers 0.000 claims abstract description 11
- 239000000126 substance Substances 0.000 claims abstract description 8
- 238000011049 filling Methods 0.000 claims description 3
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 13
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 abstract description 4
- 239000010802 sludge Substances 0.000 abstract description 4
- 239000002689 soil Substances 0.000 abstract description 3
- 239000011248 coating agent Substances 0.000 abstract description 2
- 238000000576 coating method Methods 0.000 abstract description 2
- 239000012531 culture fluid Substances 0.000 abstract 1
- 238000012856 packing Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 239000002245 particle Substances 0.000 description 7
- 238000001179 sorption measurement Methods 0.000 description 5
- 239000000843 powder Substances 0.000 description 4
- 238000009423 ventilation Methods 0.000 description 4
- 239000004372 Polyvinyl alcohol Substances 0.000 description 3
- 238000009841 combustion method Methods 0.000 description 3
- 238000004332 deodorization Methods 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000010800 human waste Substances 0.000 description 3
- 229920002451 polyvinyl alcohol Polymers 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- 239000005995 Aluminium silicate Substances 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- QYKIQEUNHZKYBP-UHFFFAOYSA-N Vinyl ether Chemical class C=COC=C QYKIQEUNHZKYBP-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000007931 coated granule Substances 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 230000003100 immobilizing effect Effects 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000009630 liquid culture Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000003415 peat Substances 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229910000160 potassium phosphate Inorganic materials 0.000 description 1
- 235000011009 potassium phosphates Nutrition 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
Description
【発明の詳細な説明】
この発明は、各種の工場又は処理施設から発生する悪臭
気体を生物学的に分解脱臭する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for biologically decomposing and deodorizing malodorous gases generated from various factories or processing facilities.
(従来技術)
下水処理場、し尿処理場等の汚水処理施設又はパルプ工
場、肥料工場等の各種工場等からは種々の有機性又は無
機性成分を含む悪臭気体が発生されている。(Prior Art) Bad-smelling gases containing various organic or inorganic components are generated from sewage treatment facilities such as sewage treatment plants and human waste treatment plants, and from various factories such as pulp factories and fertilizer factories.
而して従来の脱臭対策としては一般に臭気排出強度○E
R(0dor Emission Rate) 幾何
平均値1.7X 106Nrrf /分程度である腐敗
臭気については薬液洗浄法、酸化剤と活性炭の組合せ、
或は直接燃焼法が適用されており、5X107程度では
直接燃焼法の他、イオン交換樹脂と活性炭吸着の組合せ
によって行なわれている。Therefore, as a conventional deodorizing measure, the odor emission intensity is generally
R (0dor Emission Rate) Geometric mean value: 1.7X 106Nrrf /min For putrid odor, chemical cleaning method, combination of oxidizing agent and activated carbon,
Alternatively, a direct combustion method is applied, and in the case of about 5×107, in addition to the direct combustion method, a combination of ion exchange resin and activated carbon adsorption is used.
また、OE R2,7X 106〜5.5X 10’程
度の低濃度臭気であっても排出量が多量になってくると
燃焼法又は薬液洗浄法は有効でなく、通常は活性炭吸着
法によって行なわれているが、この方法ではアンモニア
、硫化水素、メチルアミン等の低分子臭気成分の吸着が
充分に行なわれない欠点がある。Furthermore, even if the concentration of odor is as low as OE R2.7X 106 to 5.5X 10', the combustion method or chemical cleaning method is not effective when the amount of emissions becomes large, so activated carbon adsorption method is usually used. However, this method has the disadvantage that low-molecular-weight odor components such as ammonia, hydrogen sulfide, and methylamine cannot be adsorbed sufficiently.
更に上記の各処理方法はいずれも高いコストを要し、特
に活性炭吸着法は破過後の再生壁が問題であった。Furthermore, each of the above-mentioned treatment methods requires high costs, and in particular, the activated carbon adsorption method has a problem of regenerated walls after breakthrough.
最近処理コストの低減を期待して生物脱臭法が注目され
土壌やコンポストを用いることも試みられているが、通
気抵抗が大きいため堆積高さに制限があり、従って広い
面積が必要となるので大量排気処理には不適当である。Recently, biological deodorization methods have attracted attention in hopes of reducing treatment costs, and attempts have been made to use soil or compost. However, due to the high airflow resistance, there is a limit to the height of the pile, and therefore a large area is required. Not suitable for exhaust treatment.
(目的)
本発明は臭気排出強度○ERが105〜108Nn(7
分の悪臭気体を経済的に多量処理できる脱臭方法を提供
するものである。(Purpose) The present invention has an odor emission intensity○ER of 105 to 108 Nn (7
The purpose of the present invention is to provide a deodorizing method that can economically treat large quantities of malodorous gases.
(構成)
本発明は、冷水不溶の含水性ポリマーを通気抵抗の少な
い粒径的5〜15mmの顆粒に成形し7、この顆粒表面
にその全面に付着する程度の量の中性無機物微粉末ご被
覆させたものを担体として使用するものである。(Structure) In the present invention, a water-containing polymer insoluble in cold water is molded into granules with a particle size of 5 to 15 mm with low ventilation resistance7, and a sufficient amount of neutral inorganic fine powder is attached to the surface of the granules. The coated material is used as a carrier.
冷水不溶の含水性ポリマーとしては例えば完全鹸化ポリ
ビニルアルコール、酢酸ビニルとアクリル系モノマー及
び、又はビニルエーテルとの共重合物の鹸化物、ポリビ
ニルアルコールのアクリル系モノマーのグラフト化合物
、アクリル系ポリマー、ウレタン及び水可溶性ポリマー
の架橋化物等である。Examples of water-containing polymers that are insoluble in cold water include completely saponified polyvinyl alcohol, saponified copolymers of vinyl acetate and acrylic monomers and/or vinyl ethers, graft compounds of polyvinyl alcohol and acrylic monomers, acrylic polymers, urethane, and water. These include crosslinked products of soluble polymers.
また、被覆用の微粉無機物は、微生物を阻害しないほぼ
中性の土壌、カオリン、タルク等種々の無機物質がある
が、好ましくは活性炭微粉末又はキレート効果のあるゼ
オライト微粉末であり、これらの被覆によって担体製造
後の貯蔵中におけるブロッキング又は脱臭層の自動圧密
によるブロック化が防止される。In addition, the fine inorganic substance for coating includes various inorganic substances such as almost neutral soil, kaolin, and talc that do not inhibit microorganisms, but preferably activated carbon fine powder or zeolite fine powder with chelating effect is used. This prevents blocking during storage after carrier production or blocking due to automatic compaction of the deodorizing layer.
上記の含水ポリマーは、担体表面の無機物粉末に適度な
湿度を与え微生物の増殖を促進させると共に接触した悪
臭成分の拡散を容易にする効果がある。The water-containing polymer described above has the effect of imparting appropriate humidity to the inorganic powder on the surface of the carrier, promoting the growth of microorganisms, and facilitating the diffusion of malodorous components that come into contact with it.
また、吸着又は生物分解によって副生される酸化物質の
中和反応を円滑にする効果もある。It also has the effect of smoothing the neutralization reaction of oxidized substances produced by adsorption or biodegradation.
*発明においてはポリマ・−の吸水に伴う担体粒子の膨
張作用な利用して、脱臭に作用する微生物を液体培養し
た微生物含有の培養液、或はあらかじめ脱臭に作用する
微生物を含む液に、担体粒子を浸漬することによって、
吸水時に担体粒子表面へ懸濁液中の微生物の吸着固定化
が容易に行なわれるのである。*In the present invention, the carrier particles are added to a culture solution containing microorganisms in which microorganisms that act on deodorization are cultured in liquid, or to a solution containing microorganisms that act on deodorization in advance, by utilizing the expansion effect of carrier particles as the polymer absorbs water. By dipping the particles,
When water is absorbed, microorganisms in suspension are easily adsorbed and immobilized on the surface of carrier particles.
なお、ポリマー担体の水分調整は水分低下時の担体収縮
による充填体積の減少をモニタして散水すればよい。The water content of the polymer carrier can be adjusted by sprinkling water while monitoring the decrease in the filling volume due to shrinkage of the carrier when the water content decreases.
(実施例)
直径150m+n x高さ200+umの円筒カラムに
平均粒径約10mmの微粉末活性炭被覆顆粒ポリビニル
アルコールをし尿消化汚泥中へ1昼夜どぶ漬は後1−1
150mm充填した。(充填層fit2.65ffl
)メチルメルカプタン及び硫化メチル各5ppm含有さ
せた空気を5V501(、−1,1週間通し、排出され
た空気中にメチルメルカプタン又は硫化メチルが含有さ
れていないことを確認し、馴養を完了した。(Example) In a cylindrical column with a diameter of 150 m + n x height of 200 + um, finely powdered activated carbon-coated granules of polyvinyl alcohol with an average particle size of about 10 mm were soaked in human waste digested sludge for a day and a night after 1-1.
It was filled to a depth of 150 mm. (Filled bed fit2.65ffl
) Air containing 5 ppm each of methyl mercaptan and methyl sulfide was passed through the 5V501 for 1 week, and it was confirmed that the discharged air did not contain methyl mercaptan or methyl sulfide, and acclimatization was completed.
その後、5日間通気したが排気中には両成分が検出され
ず両成分が吸着除去されていることが確認された。次に
メチルメルカプタンを10Ppm含有させた空気を5V
200Hr−’にて1ケ月通気したが、排気中に悪臭成
分が検出されず、該成分の生物分解が行なわれているこ
とが認められた。Thereafter, after aeration for 5 days, both components were not detected in the exhaust gas, and it was confirmed that both components were adsorbed and removed. Next, air containing 10 Ppm of methyl mercaptan was applied at 5 V.
Although aeration was carried out at 200 Hr-' for one month, no malodorous components were detected in the exhaust gas, indicating that the components were biodegraded.
含有成分が吸着し生物酸化された結果、担体表面が酸性
になる。これを中和するため1日1回リン酸カリ緩衡水
溶液を円筒カラムの上から散布した。As a result of adsorption and biooxidation of the contained components, the surface of the carrier becomes acidic. In order to neutralize this, a potassium phosphate buffered aqueous solution was sprayed from above the cylindrical column once a day.
(比較例1)
実施例と同様のカラムに実施例と同旦のピートモスを充
填し、石灰による中和処理後し原酒化汚泥を散布して同
様の馴養を行なったが、同様の性能を得るのに2週間必
要であった。(Comparative Example 1) A column similar to that in the example was filled with peat moss from the same day as in the example, and the same acclimatization was performed by spraying the unprocessed sludge after neutralization with lime, but the same performance was obtained. It took two weeks.
以後、通気量を増大して5V120Hr−’としたとこ
ろ、排気中にメチルメルカプタンがippm程度残留し
ており、実施例と同様の効果は得られなかった。Thereafter, when the ventilation amount was increased to 5V120Hr-', approximately ippm of methyl mercaptan remained in the exhaust gas, and the same effect as in the example could not be obtained.
(比較例2)
実施例と同様のカラムに実施例と同盟のフライアッシュ
で成型した担体をし尿消化汚泥中へ1昼夜とぶ漬は後充
填した後、同様の馴養を行なったが同様の性能を得るの
に2週間必要であった。(Comparative Example 2) A carrier molded with fly ash similar to that of the example was filled in a column similar to that of the example by soaking it in human waste digested sludge for a day and night, and then the same acclimatization was performed, but the same performance was obtained. It took two weeks to get it.
以後実施例と同様メチルメルカプタンを10ppm含有
させた空気を5V100Hr−1にて通気したが、排気
中にメチルメルカプタンおよび硫化メチルが数PPm程
度検出され、実施例と同様の効果は得られなかった。こ
の場合には担体の乾燥を防止するためポンプによって常
時充填層にシャワーをかけなければならなかった。Thereafter, air containing 10 ppm of methyl mercaptan was vented at 5 V and 100 Hr as in the example, but methyl mercaptan and methyl sulfide were detected in the exhaust gas at several ppm, and the same effect as in the example could not be obtained. In this case, it was necessary to constantly shower the packed bed with a pump to prevent the carrier from drying out.
(効果)
本発明における顆粒担体は充填筒内において通気抵抗が
少なく時間当り多重の排気を通気できる。(Effects) The granule carrier of the present invention has low ventilation resistance in the packed cylinder and can vent multiple times per hour.
また、顆粒状で各球体の不均一度が大きいので微生物棲
息面及び気体接触表面積も大きくなり、このため微生物
馴致期間が短縮されしかも高い処理能力を発揮できるの
である。In addition, since it is granular and the degree of non-uniformity of each sphere is large, the microbial habitat and gas contact surface area are also large, which shortens the microbial adaptation period and enables high processing capacity.
更に、担体が含水性ポリマーで構成されているので微生
物を棲息させるための湿度付与又は調整が容易になり、
ランニングコストを低減できる他従来法の最大問題であ
った再生を不要にできる等大きな経済効果が期待できる
ものである。Furthermore, since the carrier is composed of a water-containing polymer, it is easy to provide or adjust humidity to inhabit microorganisms.
It can be expected to have great economic effects, such as reducing running costs and eliminating the need for regeneration, which was the biggest problem with conventional methods.
さらに、膨張を伴うポリマー担体の大量の吸水作用によ
る担体表面への微生物固定化の方法を利用することで、
脱臭作用をもつ微生物の固定化による利用が容易になる
と共に、液体培養によって得られた菌体の固定化による
利用が可能となる。Furthermore, by utilizing a method of immobilizing microorganisms on the carrier surface by the action of a polymer carrier that absorbs a large amount of water accompanied by swelling,
It becomes easier to use microorganisms with a deodorizing effect by immobilization, and it also becomes possible to use microorganisms obtained by liquid culture by immobilization.
また、担体表面への微生物固定量も容易に調整できる。Furthermore, the amount of microorganisms immobilized on the carrier surface can be easily adjusted.
担体粒子充填時の空げき率が大きいので、通気時の圧力
損失が小さく、省エネルギーを達成できる。Since the void ratio when filling the carrier particles is large, the pressure loss during ventilation is small, and energy saving can be achieved.
特許出願人 デンカエンジニアリング株式会社同上 人
傑1)宏
代理人 弁理士 中村 宏Patent applicant Denka Engineering Co., Ltd. Hitoshi 1) Hiroshi Agent Patent attorney Hiroshi Nakamura
Claims (1)
性ポリマー担体を通気筒内に充填し、微生物馴養した後
、該充填層に悪臭排気を通気せしめることを特徴とする
生物脱臭方法。1. A biological deodorizing method, which comprises filling a cold water-insoluble granular water-containing polymer carrier coated with a powdery inorganic substance in a ventilating cylinder, acclimatizing it to microorganisms, and then aerating foul-smelling exhaust air through the packed bed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63091598A JPH01266835A (en) | 1988-04-15 | 1988-04-15 | Biological deodorizing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63091598A JPH01266835A (en) | 1988-04-15 | 1988-04-15 | Biological deodorizing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01266835A true JPH01266835A (en) | 1989-10-24 |
JPH0365208B2 JPH0365208B2 (en) | 1991-10-11 |
Family
ID=14030995
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63091598A Granted JPH01266835A (en) | 1988-04-15 | 1988-04-15 | Biological deodorizing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01266835A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03178316A (en) * | 1989-12-06 | 1991-08-02 | Ebara Infilco Co Ltd | Deodorizing method for offensive odor gas |
US5236677A (en) * | 1992-03-13 | 1993-08-17 | Grupo Cydsa S.A. De C.V. | Biological process for the elimination of sulphur compounds present in gas mixtures |
ES2081768A1 (en) * | 1993-06-30 | 1996-03-01 | Denka Consult & Eng | Hydrated granular carrier prepared from polyvinyl alcohol and activated charcoal for biological treatment apparatus |
JP2008048614A (en) * | 2006-08-22 | 2008-03-06 | Nisshin Foods Kk | Method for producing minced meat, and method for producing fish flour-like meat |
-
1988
- 1988-04-15 JP JP63091598A patent/JPH01266835A/en active Granted
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03178316A (en) * | 1989-12-06 | 1991-08-02 | Ebara Infilco Co Ltd | Deodorizing method for offensive odor gas |
US5236677A (en) * | 1992-03-13 | 1993-08-17 | Grupo Cydsa S.A. De C.V. | Biological process for the elimination of sulphur compounds present in gas mixtures |
ES2081768A1 (en) * | 1993-06-30 | 1996-03-01 | Denka Consult & Eng | Hydrated granular carrier prepared from polyvinyl alcohol and activated charcoal for biological treatment apparatus |
JP2008048614A (en) * | 2006-08-22 | 2008-03-06 | Nisshin Foods Kk | Method for producing minced meat, and method for producing fish flour-like meat |
JP4584207B2 (en) * | 2006-08-22 | 2010-11-17 | 日清フーズ株式会社 | Meat soba manufacturing method |
Also Published As
Publication number | Publication date |
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JPH0365208B2 (en) | 1991-10-11 |
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