JPH0394808A - Flame-retardant gas filter medium and its production - Google Patents
Flame-retardant gas filter medium and its productionInfo
- Publication number
- JPH0394808A JPH0394808A JP22986489A JP22986489A JPH0394808A JP H0394808 A JPH0394808 A JP H0394808A JP 22986489 A JP22986489 A JP 22986489A JP 22986489 A JP22986489 A JP 22986489A JP H0394808 A JPH0394808 A JP H0394808A
- Authority
- JP
- Japan
- Prior art keywords
- flame
- flame retardant
- retardant
- filter medium
- resin
- 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
- 239000003063 flame retardant Substances 0.000 title claims abstract description 82
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 title claims abstract description 71
- 238000004519 manufacturing process Methods 0.000 title claims description 17
- 229920005989 resin Polymers 0.000 claims abstract description 30
- 239000011347 resin Substances 0.000 claims abstract description 30
- 239000007789 gas Substances 0.000 claims abstract description 22
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 21
- 239000011574 phosphorus Substances 0.000 claims abstract description 21
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 20
- DHKHKXVYLBGOIT-UHFFFAOYSA-N acetaldehyde Diethyl Acetal Natural products CCOC(C)OCC DHKHKXVYLBGOIT-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229920002554 vinyl polymer Polymers 0.000 claims abstract description 12
- 150000002148 esters Chemical class 0.000 claims abstract description 11
- 239000000463 material Substances 0.000 claims abstract description 11
- 239000004114 Ammonium polyphosphate Substances 0.000 claims abstract description 9
- 235000019826 ammonium polyphosphate Nutrition 0.000 claims abstract description 9
- 229920001276 ammonium polyphosphate Polymers 0.000 claims abstract description 9
- YUWBVKYVJWNVLE-UHFFFAOYSA-N [N].[P] Chemical compound [N].[P] YUWBVKYVJWNVLE-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000007864 aqueous solution Substances 0.000 claims description 22
- 229920001187 thermosetting polymer Polymers 0.000 claims description 19
- 239000011148 porous material Substances 0.000 claims description 18
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 12
- 229910019142 PO4 Inorganic materials 0.000 claims description 11
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 11
- 239000010452 phosphate Substances 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 239000000243 solution Substances 0.000 claims description 10
- 150000001241 acetals Chemical class 0.000 claims description 8
- 239000003054 catalyst Substances 0.000 claims description 8
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 8
- 239000000047 product Substances 0.000 claims description 7
- 239000011134 resol-type phenolic resin Substances 0.000 claims description 7
- 229910017464 nitrogen compound Inorganic materials 0.000 claims description 6
- 229920000877 Melamine resin Polymers 0.000 claims description 5
- 239000004640 Melamine resin Substances 0.000 claims description 5
- 229920001807 Urea-formaldehyde Polymers 0.000 claims description 5
- 239000007795 chemical reaction product Substances 0.000 claims description 4
- 239000006185 dispersion Substances 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 239000011354 acetal resin Substances 0.000 claims description 2
- 150000002830 nitrogen compounds Chemical class 0.000 claims description 2
- 229920006324 polyoxymethylene Polymers 0.000 claims description 2
- 238000006359 acetalization reaction Methods 0.000 claims 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 claims 1
- 238000004378 air conditioning Methods 0.000 abstract description 4
- 239000000567 combustion gas Substances 0.000 abstract description 3
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 abstract description 3
- 231100000053 low toxicity Toxicity 0.000 abstract description 3
- 125000002777 acetyl group Chemical class [H]C([H])([H])C(*)=O 0.000 abstract 2
- 230000002093 peripheral effect Effects 0.000 abstract 1
- 230000003449 preventive effect Effects 0.000 abstract 1
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 14
- 230000000694 effects Effects 0.000 description 14
- 238000000034 method Methods 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 10
- 229910052736 halogen Inorganic materials 0.000 description 8
- 238000006116 polymerization reaction Methods 0.000 description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 6
- 150000002367 halogens Chemical class 0.000 description 6
- -1 phosphorus compound Chemical class 0.000 description 6
- 150000001299 aldehydes Chemical class 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000007127 saponification reaction Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 238000010998 test method Methods 0.000 description 4
- 239000003431 cross linking reagent Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 2
- ZTQSAGDEMFDKMZ-UHFFFAOYSA-N Butyraldehyde Chemical compound CCCC=O ZTQSAGDEMFDKMZ-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000010425 asbestos Substances 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 150000003014 phosphoric acid esters Chemical class 0.000 description 2
- 229920001592 potato starch Polymers 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229910052895 riebeckite Inorganic materials 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- 206010007269 Carcinogenicity Diseases 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- 229920000388 Polyphosphate Polymers 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000000740 bleeding effect Effects 0.000 description 1
- 231100000260 carcinogenicity Toxicity 0.000 description 1
- 230000007670 carcinogenicity Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 238000013007 heat curing Methods 0.000 description 1
- 239000004312 hexamethylene tetramine Substances 0.000 description 1
- 235000010299 hexamethylene tetramine Nutrition 0.000 description 1
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 1
- GTTBQSNGUYHPNK-UHFFFAOYSA-N hydroxymethylphosphonic acid Chemical compound OCP(O)(O)=O GTTBQSNGUYHPNK-UHFFFAOYSA-N 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 239000012784 inorganic fiber Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- QUBQYFYWUJJAAK-UHFFFAOYSA-N oxymethurea Chemical compound OCNC(=O)NCO QUBQYFYWUJJAAK-UHFFFAOYSA-N 0.000 description 1
- 229950005308 oxymethurea Drugs 0.000 description 1
- 125000005328 phosphinyl group Chemical group [PH2](=O)* 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 150000003018 phosphorus compounds Chemical class 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000001205 polyphosphate Substances 0.000 description 1
- 235000011176 polyphosphates Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000010517 secondary reaction Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- HGBOYTHUEUWSSQ-UHFFFAOYSA-N valeric aldehyde Natural products CCCCC=O HGBOYTHUEUWSSQ-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Filtering Materials (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、ビルの空調等に使用するn燃性気体用濾材に
係り、更に詳しくは、ポリビニルアセタール系多孔質体
よりなる難燃性気体用濾材及びその製法に関する.
(従来の技術)
高純度な清浄空気を必要とする電子工業や精密機械工業
をはじめ、ビルの空調設備等にエアーフィルター装置が
従来より広く使用されている.このエアーフィルター装
置に使用される濾材としては、無機系と有機系とが有り
、無機系では、ガラス繊維.ウィスカー.石綿(アスベ
スト)繊維等の無機系繊維の集合体が用いられ、有機系
では、合威繊維の不織布.a’s紙又はウレタン系フォ
ームあるいはポリビニルアセタール系多孔質体等が用い
られている.このうち無機系の濾材は、濾材自体の曲げ
強度や引張り強度が小さく、繊維の破損や脱落が起き易
く取扱いが困難であり、またコストが高いという欠点が
あった.さらに石綿では、最近になり発ガン性も大きな
問題となっている.一方、有機系にあっては、近年にな
り火災時の難燃性と燃焼時における有毒ガスの発生が問
題とされてきた.このため、手織布製濾材や濾紙におい
てはt1燃剤を、その製造工程中に結合剤と混合して同
時に付着させるか、もしくは単独で含浸、コーティング
する方法が行なわれている.しかし、この場合は、H燃
剤を結合剤と混合したり、単独で付着させるため、難燃
剤の添加による強力の低下や耐久性の低下、さらに難燃
剤のにじみ出しなど気体用濾材としての適性に悪影響を
与えるというrt..’tn点があった.
一般に難燃剤は、構戒或分により有機系と無機系に分頬
され、有機系は更にリン系.窒素系1ハロゲン系に分類
される.又、リン系難燃剤は更にリン酸エステル系,ポ
リリン酸塩系.リン+ハロゲン系,リン+窒素系,反応
型リン化合物.有機リン窒素化合物,無機リン化合物等
に細分頚される.ここで、添加される難燃剤がハロゲン
系又はハロゲンを含有するものであった場合、燃焼時に
ハロゲン系の有害ガスを発生し好ましくないやそこで、
有機系高分子多孔質体であるポリビニルアセタール系樹
脂の多孔質体に非ハロゲン系の難燃剤を内添又は外添す
る方法が提案されているが、tII燃剤を内添プレミン
クスする場合はかなり大量を添加しないと十分な難燃効
果を発揮せず、しかも、リン系難燃剤では難燃剤が可塑
剤としての性質を有する場合が多く、できたポリビニル
アセタール系多孔質体は、気体用濾剤としての好ましい
物性に欠けるという問題点があった.又、ポリビニルア
セタール系多孔賞に難燃剤を外添により付着含浸させた
場合は、不織布と同様のにじみ出しなどによる周辺器材
への障害の発生や難燃効果の耐久性の低下などの問題点
があった.(発明が解決しようとする課題)
本発明の目的は、ポリビニルアセタール系多孔質体を素
材としtiI燃効果の耐久性にすぐれ且つ燃焼時に発生
するガスが低毒性である難燃性気体用濾材およびその製
造方法を提供するにある.(!I8を解決するための手
段)
上記目的は、ポリビニルアセタール(以下、rPVAt
Jという)系樹脂又はその加工体の多孔質体よりなる気
体用濾材であって、前記気体用濾材にポリリン酸アンモ
ニウムj1燃剤.有機リン窒素化合物難燃剤及びリン酸
エステル系難燃剤よりなる群より選ばれた少なくとも1
種のリン系難燃剤を重量比で10〜80重量%施与する
ことを特徴とする難燃性気体用濾材にて達戒される。本
発明の他の目的は後述の方法により達威される。Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a filter medium for flammable gas used for air conditioning of buildings, etc., and more specifically relates to a filter medium for flame-retardant gas made of a polyvinyl acetal porous material. Concerning filter media and their manufacturing method. (Conventional technology) Air filter devices have been widely used in the electronics industry and precision machinery industry, which require high-purity clean air, as well as in building air conditioning equipment. There are two types of filter media used in this air filter device: inorganic and organic. Whisker. Aggregates of inorganic fibers such as asbestos fibers are used, and organic fibers include nonwoven fabrics of Hewei fibers. A's paper, urethane foam, polyvinyl acetal porous material, etc. are used. Among these, inorganic filter media have the disadvantage that the filter media themselves have low bending strength and tensile strength, are difficult to handle because fibers tend to break or fall off, and are expensive. Furthermore, the carcinogenicity of asbestos has recently become a major issue. On the other hand, in recent years, organic materials have become problematic in terms of their flame retardancy in the event of a fire and the generation of toxic gases during combustion. For this reason, in hand-woven filter media and filter paper, the T1 refueling agent is either mixed with a binder and deposited at the same time during the manufacturing process, or impregnated or coated alone. However, in this case, the H flame retardant is mixed with a binder or attached alone, resulting in a decrease in strength and durability due to the addition of the flame retardant, as well as oozing of the flame retardant, which affects its suitability as a filter medium for gases. rt. .. There were 'tn points. In general, flame retardants are divided into organic and inorganic types depending on their structure, and organic types are further divided into phosphorus types. It is classified as nitrogen type 1 halogen type. In addition, phosphorus-based flame retardants include phosphoric acid ester-based and polyphosphate-based flame retardants. Phosphorus + halogen type, phosphorus + nitrogen type, reactive phosphorus compound. It is subdivided into organic phosphorus nitrogen compounds, inorganic phosphorus compounds, etc. Here, if the added flame retardant is halogen-based or contains halogen, it will generate harmful halogen-based gas during combustion, which is undesirable.
A method has been proposed in which a non-halogen flame retardant is added internally or externally to a porous body of polyvinyl acetal resin, which is an organic polymer porous body, but when pre-minxing a tII flame retardant internally, a fairly large amount is required. If phosphorus-based flame retardants are not added, sufficient flame retardant effect will not be exhibited.Furthermore, phosphorus-based flame retardants often have properties as plasticizers, and the resulting polyvinyl acetal porous material can be used as a gas filter agent. The problem was that it lacked favorable physical properties. In addition, when a polyvinyl acetal porous material is externally added and impregnated with a flame retardant, there are problems such as damage to surrounding equipment due to oozing, similar to non-woven fabric, and a decrease in the durability of the flame retardant effect. there were. (Problems to be Solved by the Invention) An object of the present invention is to provide a flame-retardant gas filter material that is made of a polyvinyl acetal porous material, has excellent durability in the tiI flame effect, and has low toxicity in the gas generated during combustion. The purpose of this article is to provide a manufacturing method for the same. (Means for solving !I8) The above purpose is to solve polyvinyl acetal (hereinafter referred to as rPVAt).
A gas filter medium made of a porous body of a resin or a processed product thereof, which is referred to as ammonium polyphosphate J1 refueling agent. At least one selected from the group consisting of organophosphorus nitrogen compound flame retardants and phosphate ester flame retardants
This is achieved by a flame-retardant filter medium for gases, which is characterized by applying 10 to 80% by weight of a phosphorus-based flame retardant. Other objects of the invention are achieved by the method described below.
本発明において、PVA t系樹脂又はその加工体の多
孔質体とはポリビニルアルコール(以下、rPVAJと
いう)を原料とし、アルデヒド類に触媒を加えて反応さ
せた生或物で、連続した気孔を有する多孔質体であり、
その気孔率は好ましくは80%以上、更に好ましくは9
0%以上である。In the present invention, the porous body of PVA t-based resin or its processed product is a raw material made of polyvinyl alcohol (hereinafter referred to as rPVAJ) as a raw material and reacted by adding a catalyst to aldehydes, and has continuous pores. It is a porous body,
The porosity is preferably 80% or more, more preferably 9
It is 0% or more.
本発明の第1の肝要は、施与せしめる難燃剤の種類にあ
る.本発明のリン系難燃剤は、iiI燃効果の他に防錆
効果も有し、濾材に施与する方法は内添でも外添でもよ
く、また、熱硬化性樹脂と共に単独で外添する場合には
有機リン窒素化合物及びポリリン酸アンモニウムが使用
温度において昇華せず、ブリード性及びにじみ出しもほ
とんどなく、j1燃効果の耐久性に優れ好適であり、就
中ポリリン酸アンモウニムは他の難燃剤にみられない極
めてt!燃効果の優れたものであった.
又、難燃剤を熱硬化性樹脂と共に内添又は外添する場合
に用いられる難燃剤としてはリン酸エステル系龍燃剤が
好ましく、就中燃焼ガスの有害性より非ハロゲン系のリ
ン酸エステル系難燃剤が好適である.
リン系難燃剤を外添するには、浸漬やスプレーによる吹
き付け等適宜な方法でよく、PVAt系多孔質体に単に
含浸付着させてもよいし、上記リン系難燃剤と熱硬化性
樹脂の混合物を含浸付着させてもよく、その施与量はP
VA t系多孔質体に対し重量比で好ましくは10〜8
0%、より好ましくは20〜50%である.施与量が8
0%を超えると濾材の圧力損失が高くなり目詰まりを生
じる傾向があり、10%以下では難燃効果が十分でない
.
リン系難燃剤を熱硬化性樹脂と共にねり込み等の適宜な
方法で内添する場合、前述のリン系難燃剤の施与董はP
VA t系多孔質体に対し重量比で、好ましくは10〜
80%、より好ましくは40〜60%である.10%以
下では難燃効果が十分でなく、80%以上では難燃効果
が飽和したり、濾材としての物性が損なわれる傾向があ
る.本発明の第2の肝要は、リン系難燃剤を単独で用い
る他に、リン酸エステル系難燃剤を熱硬化性樹脂と共に
内添、又は外添する点にある.ここで熱硬化性樹脂とし
ては、例えば尿素樹脂,メラミン樹脂.レゾール型フェ
ノール系樹脂,エボキシ樹脂.ウレタン系樹脂等が単独
または組合わせて用いられる.
内添においては、例えば原料PVA水溶液にリン酸エス
テル系難燃剤を添加すると共に熱硬化性樹脂を添加する
方法があり、該熱硬化性樹脂としてはレゾール型フェノ
ール系樹脂が好適である.又、リン酸エステル系難燃剤
を熱硬化性樹脂と共に含浸付着等により外添する場合に
は、該熱硬化性樹脂としては尿素樹脂、又はメラミン樹
脂が好適である.
リン系W1燃剤を内添する際に、熱硬化性樹脂を同時に
添加した場合は、添加しない場合に比べリン系難燃剤の
量がより少なくても同等の難燃効果が得られる。又、リ
ン系uP.剤を熱硬化性樹脂と共に外添した場合は、し
ない場合に比べ耐水性及び耐久性がよくなる.
本発明の他の目的は、
(1)ホルマール化度が60〜86モル%であるPVA
t系多孔質体に固型分で10〜80重量%のポリリン
酸アンモニウム難燃剤又は有機リン窒素化合物til燃
剤の溶液又は分散溶液を施与した後乾燥固着せしめるか
、
(+1>ホルマール化度が60〜86モル%であるPV
At系多孔質体にリン酸エステル系難燃剤を添加した尿
素樹脂又はメラミン樹脂の水溶液を施与した後乾燥し、
引き続いて前記樹脂を熱硬化せしめるか、
(1)PVA水溶液にレゾール型フェノール系樹脂とリ
ン酸エステル系難燃剤を加えて水溶液とし、さらに気孔
形戊材、アルデヒド類及び触媒を加えて、アセタール化
反応をした後、反応生成物を水洗乾燥し、引き続いて前
記樹脂を熱硬化せしめるかする
難燃性気体用濾材の製造法によって達成される.上記(
1)の製造法における、PVAt系多孔質体のホルマー
ル化度は、好ましくは60〜86モル%,より好ましく
は、70〜86モル%.更に好ましくは80〜86モル
%である.高ホルマール化物の方が、耐水性がよく気体
用濾材として好適である.
上記(T)の製造法における、PVAt系多孔質体は、
平均重合度300〜2000の完全ケン化又は部分ケン
化のPVAを1種又は2種以上溶解した水溶液を準備し
、これに気孔形或材を加え、さらに所定量のアルデヒド
類と触媒を加えて均一ることかできる。ここで得られた
反応生成物は、ホルマール化度60〜70モル%の微細
連続気孔&lIvaを有する低ホルマール化物であり、
これをもってPVAt系多孔質体としてもよいが、再度
アルデヒド類及び酸の混液を施与してホルマール化度8
0モル%以上の高ホルマール化度とし、この高ホルマー
ル化度をもってPVAt系多孔質体とすることが好適で
ある.
上記気孔形威材としては、例えば各種澱粉類又はその膠
膨化物等が用いられる。又、アルデヒド類としては、例
えばホルムアルデヒド.アセトアルデヒド.ブチルアル
デヒド等が用いられ、触媒としては、例えば硫酸,塩酸
,リン酸等が用いられる。The first important point of the present invention lies in the type of flame retardant to be applied. The phosphorus-based flame retardant of the present invention has a rust prevention effect in addition to the III flame effect, and can be applied to the filter medium either internally or externally, or when added externally alone together with a thermosetting resin. Organic phosphorous nitrogen compounds and ammonium polyphosphate do not sublimate at the operating temperature, have almost no bleeding or oozing, and have excellent durability in J1 flame effect, making them suitable for use. I can't see it at all! It had an excellent combustion effect. In addition, when a flame retardant is added internally or externally with a thermosetting resin, phosphate ester-based flame retardants are preferable, and non-halogen phosphate ester-based flame retardants are particularly preferred due to the harmfulness of combustion gas. A fuel is preferred. To externally add the phosphorus-based flame retardant, an appropriate method such as dipping or spraying may be used, it may be simply impregnated onto the PVAt-based porous body, or a mixture of the above-mentioned phosphorus-based flame retardant and thermosetting resin may be used. It may be impregnated and attached, and the application amount is P
Preferably 10 to 8 in weight ratio to VA t-based porous material
0%, more preferably 20-50%. The dosage is 8
If it exceeds 0%, the pressure loss of the filter medium increases and tends to cause clogging, and if it is less than 10%, the flame retardant effect is not sufficient. When a phosphorus-based flame retardant is added internally with a thermosetting resin by an appropriate method such as kneading, the above-mentioned phosphorus-based flame retardant is applied to P.
Weight ratio to VA t-based porous material, preferably 10 to
80%, more preferably 40-60%. If it is less than 10%, the flame retardant effect is insufficient, and if it is more than 80%, the flame retardant effect tends to be saturated or the physical properties as a filter medium tend to be impaired. The second key point of the present invention is that in addition to using a phosphorus flame retardant alone, a phosphate ester flame retardant is added internally or externally together with the thermosetting resin. Examples of the thermosetting resin include urea resin and melamine resin. Resol type phenolic resin, epoxy resin. Urethane resins are used alone or in combination. For internal addition, for example, there is a method of adding a phosphate ester flame retardant and a thermosetting resin to the raw PVA aqueous solution, and a resol type phenolic resin is suitable as the thermosetting resin. Further, when a phosphate ester flame retardant is externally added together with a thermosetting resin by impregnation, etc., urea resin or melamine resin is suitable as the thermosetting resin. If the thermosetting resin is added at the same time as the phosphorus-based W1 flame retardant is internally added, the same flame retardant effect can be obtained even if the amount of the phosphorus-based flame retardant is smaller than when the thermosetting resin is not added. In addition, phosphorus uP. When the agent is externally added together with the thermosetting resin, water resistance and durability are improved compared to when it is not added. Other objects of the present invention are: (1) PVA having a formalization degree of 60 to 86 mol%;
A solution or dispersion of an ammonium polyphosphate flame retardant or an organic phosphorus nitrogen compound til flame retardant having a solid content of 10 to 80% by weight is applied to the T-based porous material, and then dried and fixed, or (+1> formalization degree is 60-86 mol% PV
After applying an aqueous solution of urea resin or melamine resin containing a phosphate ester flame retardant to the At-based porous material, drying it,
Subsequently, the resin is thermally cured, or (1) a resol type phenolic resin and a phosphoric acid ester flame retardant are added to the PVA aqueous solution to form an aqueous solution, and a porous wood, an aldehyde, and a catalyst are further added to acetalize the resin. This is achieved by a method for producing a flame-retardant filter medium for gases, in which after the reaction, the reaction product is washed with water, dried, and then the resin is thermally cured. the above(
In the production method of 1), the degree of formalization of the PVAt-based porous material is preferably 60 to 86 mol%, more preferably 70 to 86 mol%. More preferably, it is 80 to 86 mol%. Highly formalized materials have better water resistance and are suitable as filter media for gases. In the production method (T) above, the PVAt-based porous body is:
An aqueous solution containing one or more completely saponified or partially saponified PVA with an average degree of polymerization of 300 to 2000 is prepared, a porous material is added thereto, and a predetermined amount of aldehydes and a catalyst are added. It can be done uniformly. The reaction product obtained here is a low formalized product having fine continuous pores &lIva with a degree of formalization of 60 to 70 mol%,
This may be used as a PVAt-based porous material, but by applying a mixture of aldehydes and acids again, the degree of formalization is 8.
It is preferable to have a high degree of formalization of 0 mol% or more, and to form a PVAt-based porous body with this high degree of formalization. As the above-mentioned pore-shaped material, for example, various kinds of starches or their swollen products can be used. Examples of aldehydes include formaldehyde. Acetaldehyde. Butyraldehyde or the like is used, and as a catalyst, for example, sulfuric acid, hydrochloric acid, phosphoric acid, etc. are used.
上記(1)の製造法におけるリン系難燃剤としては、好
ましくは有機リン窒素化合物、より好ましくはポリリン
酸アンモニウムが用いられ、水溶液中の難燃剤濃度は、
好ましくは5〜40重量%、より好ましくはl5〜30
重遣%である.前述の(n)の製造法におけるPVAt
系多孔質体は、ホルマール化度が、好ましくは40〜8
6モル%、、より好ましくは70〜86モル%であり、
(1)製造法に記載したのと同様の方法で得ることがで
きる,ただし、熱硬化性樹脂を施与するため、高ホルマ
ール化物でなくてもよいのでホルマール化反応は■度で
十分である.(II)の製造法における尿素樹脂又は、
メラミン樹脂の水溶液濃度は、好ましくは10〜35重
量%、より好ましくは20〜30重量%である.樹脂濃
度が高過ぎると、できた多孔質体が硬過ぎて折り曲げ加
工がしに<<、低過ぎると濾材としての耐水性が不足す
る傾向がある.
又、(ff)の製造法において用いられる難燃剤は、樹
茄との反応性より非ハロゲン系のリン酸エステル系難燃
剤が好適であり、その水溶液濃度は好ましくは10〜3
5重量%で、より好ましくは20〜30重量%である.
(U)の製造法における熱処理温度は、好ましくは11
0〜150℃、より好ましくは120〜140℃であり
、熱処理時間は、好ましくは3〜20時間、より好まし
くは5〜l5時間である.前述の(Iff)の製造法に
おける難燃性多孔質体は平均重合度300〜2000の
完全ケン化又は部分ケン化のPVAIOO!1部に対し
、レゾール型フェノール系樹脂を好ましくは50〜16
0重量部、より好ましくは100〜140重量部混合し
、難燃剤として非ハロゲン系のリン酸エステル系¥l燃
剤を、好ましくは30〜100重量部、より好ましくは
40〜80重量部溶解した水溶液を準備し、これに気孔
形戒材を加え、さらに所定量40時間反応を行ない、反
応生成物を水洗し乾燥した後、1 1 0−1 5 0
’tテ3〜2 0時1”jl ? 処Flすることによ
り得ることができる。ここでレゾール型フェノール系樹
脂の添加量が多過ぎる場合には、できた多孔質体が硬過
ぎて折り曲げ加工がしに<<、少な過ぎる場合には耐水
性が不足する.(効果)
本発明の難燃性気体用濾材によれば、難燃性の優れた、
火災による燃焼において低発煙性かつ燃焼ガスが低毒性
であり、また、目詰り圧損上昇も少なく、防錆効果もあ
りさらに難燃剤のにしみ出しなどによる周辺器材への障
害もないので、ビル空調等に極めて好適なエアーフィル
ター装置を作製することができる.
本発明の方法によれば、PVAt系樹脂の多孔質体に施
与するリン系難燃剤の難燃効果を極めて有効に活用でき
、耐水性・耐久性・耐候性にも優れ、気体用濾材として
好適な物性をもっ難燃性気体用濾材を製造することがで
きる.
(実施例−1)
重合度1400,ケン化度99モル%の完全ケン化PV
Aと、重合度50o.ケン化度88モル%の部分ケン化
PVAとを7/3の割合で混合し、濃度IO重量%の水
溶液を600重量部作戒する。As the phosphorus-based flame retardant in the production method (1) above, preferably an organic phosphorus nitrogen compound, more preferably ammonium polyphosphate is used, and the flame retardant concentration in the aqueous solution is:
Preferably 5-40% by weight, more preferably 15-30%
It is weighted percentage. PVAt in the production method of (n) above
The degree of formalization of the porous body is preferably 40 to 8.
6 mol%, more preferably 70 to 86 mol%,
(1) It can be obtained by the same method as described in the manufacturing method. However, since a thermosetting resin is applied, it does not need to be a highly formalized product, so a formalization reaction of 1 degree is sufficient. .. The urea resin in the manufacturing method of (II) or
The concentration of the melamine resin in the aqueous solution is preferably 10 to 35% by weight, more preferably 20 to 30% by weight. If the resin concentration is too high, the resulting porous body will be too hard and difficult to bend, and if it is too low, it will tend to lack water resistance as a filter medium. In addition, the flame retardant used in the production method of (ff) is preferably a non-halogen phosphate ester flame retardant due to its reactivity with the tree, and the concentration of the aqueous solution thereof is preferably 10 to 3.
It is 5% by weight, more preferably 20 to 30% by weight. The heat treatment temperature in the manufacturing method of (U) is preferably 11
The temperature is 0 to 150°C, more preferably 120 to 140°C, and the heat treatment time is preferably 3 to 20 hours, more preferably 5 to 15 hours. The flame-retardant porous material in the above-mentioned manufacturing method (Iff) is completely saponified or partially saponified PVAIOO! with an average degree of polymerization of 300 to 2000. Preferably 50 to 16 parts of resol type phenolic resin to 1 part
An aqueous solution containing 0 parts by weight, more preferably 100 to 140 parts by weight, and preferably 30 to 100 parts by weight, more preferably 40 to 80 parts by weight of a non-halogenated phosphate ester flame retardant dissolved therein. was prepared, porous wood was added thereto, the reaction was further carried out for a prescribed amount of 40 hours, the reaction product was washed with water and dried, and 110-150
It can be obtained by processing 3 to 20 o'clock 1" jl? If the amount of resol type phenolic resin added is too large, the resulting porous body will be too hard and cannot be bent. If the amount is too low, the water resistance will be insufficient. (Effect) According to the flame-retardant gas filter medium of the present invention,
When burned in a fire, the smoke emission is low, the combustion gas is low toxicity, there is little increase in pressure loss due to clogging, there is a rust prevention effect, and there is no problem with surrounding equipment due to flame retardant seeping out, so it is suitable for building air conditioning. It is possible to create an air filter device that is extremely suitable for such applications. According to the method of the present invention, the flame retardant effect of the phosphorus flame retardant applied to the porous body of PVAt resin can be utilized extremely effectively, and it has excellent water resistance, durability, and weather resistance, and can be used as a filter medium for gases. A flame-retardant gas filter medium with suitable physical properties can be manufactured. (Example-1) Completely saponified PV with a degree of polymerization of 1400 and a degree of saponification of 99 mol%
A and a polymerization degree of 50o. Partially saponified PVA with a degree of saponification of 88 mol % was mixed at a ratio of 7/3, and 600 parts by weight of an aqueous solution having a concentration of IO weight % was prepared.
この水溶液に気孔形威材として30重量%の馬鈴薯澱粉
スラリーを100重量部加えて撹拌混合し、さらに架橋
剤として37%ホルムアルデヒド水溶液をt00重量部
加えると共に、触媒として50%梳酸を100重量部加
えて均一に混合し、反応液を調整する.この調整液を8
0’Cでl8時間反応を行ない、ホルマール化度60〜
70モル%のPVAt系樹脂の多孔質体とする.引き続
き、この多孔質体瓢20%ホルマリンと25%硫酸との
混液に遥壇レて、温度60℃で、150時間2次反応を
行ない、ホルマール化度80〜86モル%のPVAL系
樹脂の多孔質体とする.そして、この多孔質体を水洗、
乾燥して厚さ2mmに切断し、切断した多孔質体に難燃
剤としてポリリン酸アンモニウム(商品名:スミセーフ
Pく住友化学工業n製〉)の20%水溶液を付着.含浸
させ、これを乾燥し、固形分重量比で50重量%の難燃
剤が施与された多孔質濾村を得た.次いで、下記方法に
より得られた多孔質濾科の難燃製試験を行なった.
(^)JACA N0.11−1977r空気清浄装
置用濾勅燃焼性試験方法」に準じ、金網上の試験片25
0mm’.8 250mmの表面中央で0. 1.
5 gのへキサミン錠剤を火源として燃焼し、最大炭化
長を測定した所25mm以下であり、難燃性濾材の評価
値150mm以下に合格した.
(B) ASTM D6 3 5 rF
lams. of I?tgidPlastics
over O.1 2 7 am (0.0 5
0 i n)in ThickJ.に準じ、試験片12
.7mmxl27mmを水平保持(巾方向45”)L、
ブンゼンバーナーに30秒間接炎し、燃焼距離を測った
所39mm以下であり、自己消火性の評価値70mm以
下に合格した.
(実施例−2)
重合度1500,ケン化度95〜97モル%の部分ケン
化PVAと重合度500,ケン化度99モル%の完全ケ
ン化PVAを6/4の割合で混合し、濃度10重量%の
水溶液を800重量部作戊する.この水溶液に気孔形成
材として25重置%の馬鈴薯R粉スラリーを200重量
部加えて撹拌混合し、さらに架橋剤として37%ホルム
アルデヒド水溶液を150重量部加えると共に、触媒と
して50%硫酸を100重量部加えて均一に混合し、反
応液を調整する.この調整液を80℃で18時間反応を
行ない、PVAt系樹脂の多孔質体とする.この多孔質
体を水洗、乾燥して厚さ2mmに切断し、切断した多孔
質体を熱硬化性樹脂としてジメチロール尿素を15重景
%及びH燃剤としてジプチルヒドロオキシメチルホスホ
ネート(商品名:CR−707 <大八化学製〉)を3
0重量%となるように調整された水溶液に浸漬し、余剰
の水溶液を除去した後乾燥して130℃で10時間熱硬
化反応をさせ、多孔質濾材を得た.次いで、下記方法に
より得られた多孔質濾材の難燃性試験を行なった。To this aqueous solution, 100 parts by weight of 30% by weight potato starch slurry was added as a pore-forming material and mixed with stirring, further 100 parts by weight of 37% formaldehyde aqueous solution was added as a crosslinking agent, and 100 parts by weight of 50% combing acid was added as a catalyst. Add and mix evenly to prepare the reaction solution. Add this adjustment solution to 8
The reaction was carried out at 0'C for 18 hours, and the degree of formalization was 60~
A porous body made of 70 mol% PVAt-based resin. Subsequently, this porous body was placed in a mixture of 20% formalin and 25% sulfuric acid for a secondary reaction at a temperature of 60°C for 150 hours to form a porous PVAL resin with a degree of formalization of 80 to 86 mol%. It is a matter of substance. Then, wash this porous body with water,
The porous body was dried and cut to a thickness of 2 mm, and a 20% aqueous solution of ammonium polyphosphate (trade name: Sumisaf P manufactured by Sumitomo Chemical Co., Ltd.) was applied as a flame retardant to the cut porous body. This was impregnated and dried to obtain a porous filter coated with 50% by weight of flame retardant based on solid content. Next, a flame retardant test was conducted on the porous filter obtained by the following method. (^) Test piece 25 on a wire mesh according to JACA No.11-1977r Filter flammability test method for air purifier
0mm'. 8 0.0 at the center of the 250mm surface. 1.
5 g of hexamine tablets were burned as a fire source, and the maximum carbonization length was measured to be 25 mm or less, passing the evaluation value of 150 mm or less for a flame-retardant filter medium. (B) ASTM D6 3 5 rF
lams. Of I? tgidPlastics
over O. 1 2 7 am (0.0 5
0 in) in ThickJ. Test piece 12 according to
.. 7mmxl27mm held horizontally (width direction 45”) L,
The flame was placed on a Bunsen burner for 30 seconds, and the combustion distance was measured to be 39 mm or less, passing the self-extinguishing evaluation value of 70 mm or less. (Example-2) Partially saponified PVA with a polymerization degree of 1500 and a saponification degree of 95 to 97 mol% and completely saponified PVA with a polymerization degree of 500 and a saponification degree of 99 mol% were mixed at a ratio of 6/4, and the concentration Prepare 800 parts by weight of a 10% by weight aqueous solution. To this aqueous solution, 200 parts by weight of 25% Potato R powder slurry as a pore forming material was added and mixed with stirring, further 150 parts by weight of 37% formaldehyde aqueous solution was added as a crosslinking agent, and 100 parts by weight of 50% sulfuric acid was added as a catalyst. Add and mix evenly to prepare the reaction solution. This prepared solution was reacted at 80°C for 18 hours to form a porous body of PVAt resin. This porous body was washed with water, dried and cut into 2 mm thick pieces, and the cut porous body was treated with 15% dimethylol urea as a thermosetting resin and diptyl hydroxymethyl phosphonate (trade name: CR) as a H reagent. -707 <Daihachi Chemical>) 3
It was immersed in an aqueous solution adjusted to have a concentration of 0% by weight, and after removing the excess aqueous solution, it was dried and subjected to a heat curing reaction at 130° C. for 10 hours to obtain a porous filter medium. Next, a flame retardancy test was conducted on the porous filter medium obtained by the following method.
JIS L 1091r繊維製品の燃焼゜性試験法
」のA法(燃焼試験)のA−1法(45°ミクロバーナ
ー法)で試験した所、1分間加熱で炭化面積30cm”
以下、残炎時間3秒以下、残しん時間5秒以下、炭化距
M 2 0 c m以下で、同試験法で最も難燃性の優
れた区分3に合格した.(実施例−3)
重合度L750.ケン化度88モル%のPVAの10重
量%水溶液を500重量部作威する.この水溶液に気孔
形成材として10重景%の馬鈴薯澱粉スラリーを300
frf部加え、これに熱硬化性樹脂として70重量%水
溶性レゾール型フ五ノール系樹脂を80重量部と難燃剤
としてグリシジルーα−メチルーβ−ジ(ブト▲キシ)
ホスフィニルブロビネート(商品名:CR−705 <
大八化学製〉)を30重量部加え撹拌混合し、さらに架
橋剤として37%ホルムアルデヒド水溶液を100重量
部加えると共に、触媒として38%塩酸を30重量部加
えて均一に混合し、反応液を調整する。この調整液を7
0℃で18時間反応を行ない、PVAt系樹脂の多孔質
体とする.そしてこの多孔質体を水洗.乾燥し、130
℃で18時間熱硬化反応させた後、厚さ2mmに切断し
、多孔質濾材を得た.次いで得られた多孔譬濾材の難燃
性試験を下記方法により行なった.
UL規格(米国火災保険業組合)の難燃性試験法UL−
94HF−1に準じて、規定の形状の試験片にバーナー
の炎を60秒あてて取り去った所、残炎継続時間が10
秒以下、燃焼距離が57.2mm以′下の基準に合格し
た。When tested using method A (flammability test) A-1 (45° micro burner method) of JIS L 1091r flammability test method for textile products, the carbonized area was 30 cm after heating for 1 minute.
The afterflame time was 3 seconds or less, the residual flame time was 5 seconds or less, and the carbonization distance was 20 cm or less, passing Category 3, which is the most excellent flame retardant in the same test method. (Example-3) Degree of polymerization L750. Prepare 500 parts by weight of a 10% by weight aqueous solution of PVA with a degree of saponification of 88 mol%. To this aqueous solution was added 300% of potato starch slurry containing 10% of pores as a pore-forming material.
frf part, and 80 parts by weight of a 70% by weight water-soluble resol type phenolic resin as a thermosetting resin and glycidyl-α-methyl-β-di(but▲xy) as a flame retardant.
Phosphinyl brobinate (trade name: CR-705 <
Daihachi Chemical Co., Ltd.>) was stirred and mixed, 100 parts by weight of 37% formaldehyde aqueous solution was added as a crosslinking agent, and 30 parts by weight of 38% hydrochloric acid was added as a catalyst and mixed uniformly to prepare the reaction solution. do. Add this adjustment solution to 7
The reaction was carried out at 0°C for 18 hours to form a porous body of PVAt-based resin. Then, wash this porous body with water. Dry, 130
After carrying out a thermosetting reaction at ℃ for 18 hours, the material was cut to a thickness of 2 mm to obtain a porous filter medium. Next, a flame retardant test of the obtained porous filter material was conducted using the following method. UL standard (United States Fire Insurance Association) flame retardant test method UL-
According to 94HF-1, when a burner flame was applied to a test piece of a specified shape for 60 seconds and then removed, the afterflame duration was 10.
It passed the criteria of less than 2 seconds and a combustion distance of less than 57.2 mm.
Claims (4)
孔質体よりなる気体用濾材であって、前記気体用濾材に
ポリリン酸アンモニウム難燃剤、有機リン窒素化合物難
燃剤及びリン酸エステル系難燃剤よりなる群より選ばれ
た少なくとも1種のリン系難燃剤を重量比で10〜80
重量%施与することを特徴とする難燃性気体用濾材。(1) A gas filter medium made of a porous body of polyvinyl acetal resin or a processed product thereof, wherein the gas filter medium is made of an ammonium polyphosphate flame retardant, an organophosphorus nitrogen compound flame retardant, and a phosphate ester flame retardant. At least one phosphorus-based flame retardant selected from the group 10 to 80% by weight
A flame-retardant filter medium for gas, characterized in that it is applied in a weight percent.
ニルアセタール系多孔質体に、固型分で10〜80重量
%のポリリン酸アンモニウム難燃剤又は有機リン窒素化
合物難燃剤の溶液又は分散溶液を施与した後、乾燥固着
することを特徴とする難燃性気体用濾材の製造方法。(2) A solution or dispersion of an ammonium polyphosphate flame retardant or an organic phosphorus nitrogen compound flame retardant with a solid content of 10 to 80% by weight is added to a polyvinyl acetal porous body with a degree of formalization of 60 to 86 mol%. A method for producing a flame-retardant gas filter medium, which comprises drying and fixing the material after application.
ニルアセタール系多孔質体にリン酸エステル系難燃剤を
添加した尿素樹脂又はメラミン樹脂の溶液又は分散溶液
を施与した後乾燥し、引き続いて前記樹脂を熱硬化せし
めることを特徴とする難燃性気体用濾材の製造方法。(3) A solution or dispersion of a urea resin or melamine resin containing a phosphate ester flame retardant is applied to a polyvinyl acetal porous material having a degree of formalization of 40 to 86 mol%, followed by drying. A method for producing a flame-retardant gas filter medium, which comprises thermosetting the resin.
ール系樹脂とリン酸エステル系難燃剤を加え水溶液とし
、さらに気孔形成材、アルデヒド類及び触媒を加えてア
セタール化反応した後、反応生成物を水洗乾燥し、引き
続いて前記樹脂を熱硬化せしめることを特徴とする難燃
性気体用濾材の製造方法。(4) A resol-type phenolic resin and a phosphate ester flame retardant are added to an aqueous polyvinyl alcohol solution to form an aqueous solution, and a pore-forming material, aldehydes, and a catalyst are added to carry out an acetalization reaction, and the reaction product is washed with water and dried; A method for producing a flame-retardant gas filter medium, which comprises subsequently thermosetting the resin.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22986489A JPH0394808A (en) | 1989-09-05 | 1989-09-05 | Flame-retardant gas filter medium and its production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22986489A JPH0394808A (en) | 1989-09-05 | 1989-09-05 | Flame-retardant gas filter medium and its production |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0394808A true JPH0394808A (en) | 1991-04-19 |
Family
ID=16898895
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22986489A Pending JPH0394808A (en) | 1989-09-05 | 1989-09-05 | Flame-retardant gas filter medium and its production |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0394808A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007130632A (en) * | 2005-10-14 | 2007-05-31 | Toray Ind Inc | Filtering medium and filter |
JP2016501713A (en) * | 2012-11-12 | 2016-01-21 | ネーナー・ゲスナー・ゲーエムベーハー | Flame retardant gas filter material with high dust storage capacity |
-
1989
- 1989-09-05 JP JP22986489A patent/JPH0394808A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007130632A (en) * | 2005-10-14 | 2007-05-31 | Toray Ind Inc | Filtering medium and filter |
JP2016501713A (en) * | 2012-11-12 | 2016-01-21 | ネーナー・ゲスナー・ゲーエムベーハー | Flame retardant gas filter material with high dust storage capacity |
US10293290B2 (en) | 2012-11-12 | 2019-05-21 | Neenah Gessner Gmbh | Flame-retardant gas filter material having high dust storage capacity |
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