JPS6152732B2 - - Google Patents
Info
- Publication number
- JPS6152732B2 JPS6152732B2 JP54144594A JP14459479A JPS6152732B2 JP S6152732 B2 JPS6152732 B2 JP S6152732B2 JP 54144594 A JP54144594 A JP 54144594A JP 14459479 A JP14459479 A JP 14459479A JP S6152732 B2 JPS6152732 B2 JP S6152732B2
- Authority
- JP
- Japan
- Prior art keywords
- fan
- harmful gas
- alkali
- cement material
- activated carbon
- 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.)
- Expired
Links
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
-
- 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
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Direct Air Heating By Heater Or Combustion Gas (AREA)
Description
【発明の詳細な説明】
本発明は室内排気型のフアン付暖房機の改良に
関し、暖房機の運転に伴つて室内に発生する二酸
化窒素(NO2)、一酸化炭素(CO)を除去して清
浄な暖房を行なうことを目的とする。[Detailed Description of the Invention] The present invention relates to an improvement of an indoor exhaust type fan-equipped heater, which removes nitrogen dioxide (NO 2 ) and carbon monoxide (CO) that are generated indoors when the heater is operated. The purpose is to provide clean heating.
最近は、ポータブル石油ストーブ並の手軽さで
どこにでも設置ができて温風によつて快適な暖房
が得られるフアン付暖房機が注目され、各家庭で
使用されるようになつてきた。しかし、このフア
ン付暖房機の燃焼器は、小型で発熱量が大きいた
め火炎温度が高く、しかも一次空気量の少ない拡
散燃焼法のものが主体であるためNOxの発生量
が多く、室内のNOx濃度は非常に高くなる。こ
のNOx、とくにNO2は閉塞性呼吸障害を起こすこ
とが知られており、従つて環境基準値(0.04〜
0.06ppm)を設定してこのNO2を規制している。
さらに、点火時、消火時にはCOが発生しやすい
ので、これらを除去した清浄な暖房が望まれる。 Recently, fan-equipped heaters that are as easy to install as portable kerosene stoves, can be installed anywhere, and provide comfortable heating with hot air have been attracting attention and are being used in households. However, the combustor of this fan-equipped heater is small and generates a large amount of heat, resulting in a high flame temperature.Furthermore, since it mainly uses the diffusion combustion method with a small amount of primary air, it generates a large amount of NOx. The concentration will be very high. This NOx, especially NO 2 , is known to cause obstructive breathing disorders, and therefore the environmental standard value (0.04~
0.06ppm) to regulate this NO 2 .
Furthermore, since CO is likely to be generated when igniting and extinguishing, it is desirable to have clean heating that removes these.
従来の空気清浄装置としては、電気集塵機や活
性炭フイルターなどを主体としたものがあるが、
これらは浮遊微粒子、煙などは除去できるが、上
述の最も健康に及ぼす影響が心配されているCO
は除去できなかつた。また、活性炭はNO2を吸着
によりわずかに除去できるが、その除去容量が小
さく、又高温になると脱離したり、吸着したNO2
をNOに還元してNOを放出したりする欠点があ
る。 Conventional air purification devices mainly include electrostatic precipitators and activated carbon filters, but
These can remove airborne particles, smoke, etc., but CO2, which is most concerned about the health effects mentioned above, can be removed.
could not be removed. In addition, activated carbon can remove a small amount of NO 2 by adsorption, but its removal capacity is small, and at high temperatures, it may desorb or adsorbed NO 2
It has the disadvantage of reducing NO to NO and releasing NO.
COを除去できるものとしては、酸化銅と二酸
化マンガンを主成分とする金属酸化物の混合物で
あるホプラカイト触媒や、活性炭や活性アルミナ
に白金、パラジウムなどの貴金属を担持させた触
媒が提案されている。しかし、ホプカライト触媒
は水分の存在下では活性(CO除去率)が低下す
る。 Hoplacite catalysts, which are a mixture of metal oxides whose main components are copper oxide and manganese dioxide, and catalysts in which precious metals such as platinum and palladium are supported on activated carbon or activated alumina have been proposed to remove CO. . However, the activity (CO removal rate) of the hopcalite catalyst decreases in the presence of moisture.
また、貴金属担持触媒は高温でないと使用でき
ないので実用的ではなかつた。 In addition, noble metal supported catalysts cannot be used unless they are at high temperatures, so they are not practical.
本発明は常温で、しかも水分の存在下でもCO
やNO2を除去するフイルターをフアン付暖房機に
装着して室内に排出されるNO2やCOを除去して
快適な暖房ができるようにしたものである。 The present invention enables CO2 to be released even at room temperature and in the presence of moisture.
A filter that removes NO 2 and NO 2 is attached to a heater with a fan to remove NO 2 and CO that are emitted into the room and provide comfortable heating.
第1図は空気清浄機能を有するフイルターをフ
アン付暖房機に応用した一例である。 Figure 1 is an example of a filter with an air purifying function applied to a heater with a fan.
図中、1は温風吹出フアン2の空気吸い込み口
に設置した有害ガス除去フイルター、3は燃焼
器、4は温風吹出口である。燃焼器3で燃焼した
排ガスによる温風は吹出口4より室内に吹出さ
れ、室内を暖房した後、送風機3により空気吸い
込み口の有害ガス除去フイルターを通過して清浄
になり再び室内に吹出される。有害ガス除去フイ
ルター1はアルカリとセメント材と粉末活性炭の
混練成型物よりつくられたNO2除去剤と、アルカ
リ、セメント材及び粉末活性炭との混練成型物に
貴金属を担持させたCO酸化触媒体を同時もしく
は単独に設置した構成である。 In the figure, 1 is a harmful gas removal filter installed at the air intake port of a hot air blowing fan 2, 3 is a combustor, and 4 is a hot air blowing port. Warm air from the exhaust gas burned in the combustor 3 is blown into the room from the outlet 4, heating the room, and then passed through the harmful gas removal filter at the air intake port by the blower 3, purified, and blown into the room again. . Harmful gas removal filter 1 includes an NO 2 removing agent made from a kneaded molded product of alkali, cement material, and powdered activated carbon, and a CO oxidation catalyst made by supporting a precious metal on the kneaded molded product of alkali, cement material, and powdered activated carbon. This configuration can be installed simultaneously or independently.
NO2はアルカリを用いることにより、これを硝
酸塩あるいは亜硝酸塩としてたやすく吸収するこ
とができる。このNO2除去に用いられるアルカリ
としてはKOH,NaOH,Ca(OH)2などの水酸化
化合物やK2CO3,Na2CO3,NaHCO3などの炭酸
塩の他、チオ硫酸ナトリウム、尿素など数多くの
種類がある。これらの反応はいずれも液相反応で
あり、水分の存在下でのイオン反応を中心とした
化学吸収反応である。NO2を湿式で吸収させる場
合には、水滴の飛散を防止する必要から空間速度
を上げて操作することができないなど操作性、メ
インテナンスが極めて悪い。そこで本発明者らは
アルカリと粉末活性炭をセメント材で固化して造
粒した組成物が、常温でNO2の除去に優れた性能
を有することを見出した。第2図に炭酸カリウ
ム/水酸化カルシウム/硫酸カルシウム(焼石こ
う)/粉末活性炭を重量比で3/3/2/2に配
合して混練成型した組成物のNO2除去性能の一例
を示す。これは上記組成物を3mm径で押出し成型
した造粒品の空間速度(SV)により、NO2の除
去性能がどう変化するかを示したものである。な
お、条件はNO2の入口濃度1.0〜1.2ppm、温度30
℃、相対湿度52%とした。本組成物はNO2と下記
のような反応でNO2を吸収除去するものである。 NO 2 can be easily absorbed as nitrate or nitrite by using an alkali. The alkalis used for this NO 2 removal include hydroxide compounds such as KOH, NaOH, and Ca(OH) 2 , carbonates such as K 2 CO 3 , Na 2 CO 3 , and NaHCO 3 , as well as sodium thiosulfate and urea. There are many types. All of these reactions are liquid phase reactions, and are chemical absorption reactions centered on ionic reactions in the presence of water. When NO 2 is absorbed using a wet method, operability and maintenance are extremely poor, as it is impossible to increase the space velocity due to the need to prevent water droplets from scattering. Therefore, the present inventors have discovered that a composition obtained by solidifying an alkali and powdered activated carbon with a cement material and granulating it has excellent performance in removing NO 2 at room temperature. FIG. 2 shows an example of the NO 2 removal performance of a composition prepared by kneading and molding potassium carbonate/calcium hydroxide/calcium sulfate (calcined gypsum)/powdered activated carbon in a weight ratio of 3/3/2/2. This shows how the NO 2 removal performance changes depending on the space velocity (SV) of a granulated product obtained by extrusion molding the above composition to a diameter of 3 mm. The conditions are: NO 2 inlet concentration 1.0 to 1.2 ppm, temperature 30
°C and relative humidity of 52%. This composition absorbs and removes NO 2 through the following reaction with NO 2 .
6NO2+K2CO3+2Ca(OH)2→KNO3+Ca
(NO3)2
+KNO2+Ca(NO2)2
+2H2O+CO2
2N2O3+K2CO3+Ca(OH)2→2KNO2+Ca
(NO2)2
+H2O+CO2
上述のように本組成物はNO2を高い除去率で除
去し、しかもこの除去が吸収反応であるため、長
寿命で、かつNO2→NOへの還元性がないなど従
来にない優れたものである。 6NO 2 +K 2 CO 3 +2Ca(OH) 2 →KNO 3 +Ca
(NO 3 ) 2 +KNO 2 +Ca(NO 2 ) 2 +2H 2 O+CO 2 2N 2 O 3 +K 2 CO 3 +Ca(OH) 2 →2KNO 2 +Ca
(NO 2 ) 2 + H 2 O + CO 2 As mentioned above, this composition removes NO 2 at a high removal rate, and since this removal is an absorption reaction, it has a long life and has a good ability to reduce NO 2 → NO. This is an unprecedented and superior feature, as it does not have any cracks.
また本発明者らは常温で環境濃度レベルのCO
を浄化する方法としてアルカリ、粉末活性炭及び
セメント材の3者を混練成型して、これに白金、
ロジウム、ルテニウムのいずれかの貴金属をパラ
ジウムとともに担持させるかあるいはパラジウム
単独で担持させた触媒が水蒸気共存下の一般大気
条件下で優れた性能と耐久性を有することを見出
し提案した。 The inventors also discovered that CO at an environmental concentration level at room temperature.
As a method of purifying , platinum,
We have discovered and proposed that catalysts supported with either rhodium or ruthenium, together with palladium, or palladium alone, have excellent performance and durability under general atmospheric conditions in the coexistence of water vapor.
その1実施例である、炭酸カリウム/粉末活性
炭/アルミン酸石灰を重量比で1/3/6とした
混練成型物を担体として、これに白金、パラジウ
ムを各々担体に0.3重量%担持させた触媒Aの性
能を第3図に示す。なお、触媒Aの活性評価条件
としては、15℃で飽和の絶対水分量一定の湿度条
件であり、空間速度SV=50000hr-1の条件下で、
入口CO濃度を100ppmとして測定した。第3図
では、触媒充填層温度を変化させた場合の温度と
CO転換率との関係を示した。 One example of this is a catalyst in which a kneaded molded product of potassium carbonate/powdered activated carbon/aluminate lime in a weight ratio of 1/3/6 is used as a carrier, and 0.3% by weight of each of platinum and palladium is supported on the carrier. The performance of A is shown in Figure 3. In addition, the activity evaluation conditions for catalyst A were saturated at 15°C, humidity conditions with constant absolute water content, and space velocity SV = 50000 hr -1 .
Measurements were made with an inlet CO concentration of 100 ppm. Figure 3 shows the temperature and temperature when changing the catalyst packed bed temperature.
The relationship with CO conversion rate was shown.
また、従来の活性炭に0.5重量%のパラジウム
を担持させた市販触媒Bの同等条件下での性能も
比較のために示した。この第3図から明らかな如
くA,B両者は触媒活性が著しく異なる。従来の
ホプカライト系触媒などは、水分の全くない条件
では、高性能を示すが、ここに取上げている条件
では全く転換率を示さなかつた。 Furthermore, the performance of commercially available catalyst B, in which 0.5% by weight of palladium was supported on conventional activated carbon, under the same conditions is also shown for comparison. As is clear from FIG. 3, both A and B have significantly different catalytic activities. Conventional hopcalite-based catalysts exhibit high performance under conditions where there is no moisture, but under the conditions discussed here they did not show any conversion rate.
以上に述べた2種類の組成物の併用構成、又は
単独の構成によつて燃焼排ガスによる室内の
CO,NO2の除去が可能となる。 By combining the two types of compositions described above or by using them alone, indoor air pollution caused by combustion exhaust gas can be achieved.
CO and NO 2 can be removed.
なお、これらの有害ガス除去率は、水蒸気共存
下の常温一般大気条件下で優れた性能を有するの
でフアン付暖房機の場合にはフアンの空気吸い込
み口に設置することが望ましい。温風吹出口への
設置では100℃程度に加熱されるので、組成物中
の粉末活性炭が加熱により燃焼することも考えら
れるので避けなければならない。 Note that these harmful gas removal rates have excellent performance under normal temperature general atmospheric conditions in the coexistence of water vapor, so in the case of a heater with a fan, it is desirable to install it at the air intake port of the fan. When installed at a hot air outlet, it will be heated to about 100°C, so it is possible that the powdered activated carbon in the composition will burn due to heating, which must be avoided.
また、これらの有害ガス除去剤をフアンの空気
吸い込み口に設置する場合は、粉じんなどによつ
て多孔質の表面を閉塞することもあるので、除じ
んフイルターの後方に配置することが望ましい。
具体的な充填方法としては適当な枠体に充填すれ
ばよいが、空気流のチヤンネリングを起こすこと
がないように均一化を配慮する必要がある。例え
ばその一例としてポリプロピレンなどの不織布で
有害ガス除去剤をはさんでサンドイツチ構造とす
るような、従来公知の方法がよい。 Furthermore, when installing these harmful gas removers at the air intake port of the fan, it is desirable to place them behind the dust removal filter, since the porous surface may be clogged with dust.
As for a specific filling method, it may be sufficient to fill a suitable frame, but it is necessary to take care to ensure uniformity so as not to cause channeling of the air flow. For example, a conventionally known method may be used, such as sandwiching the harmful gas removing agent between nonwoven fabrics such as polypropylene to form a sandwich structure.
このポリプロピレンは吸湿率が非常に小さいと
云うすぐれた特性を持つているので、水蒸気共存
下で優れた性能を有する前述のNO2除去剤、CO
酸化触媒をはさんでサンドイツチ構造にすると、
ポリプロピレン不織布とNO2除去剤、CO酸化触
媒の間に空気中の水分がたまりやすくなるので性
能が大巾に向上する。 This polypropylene has the excellent property of having a very low moisture absorption rate, so it can be used as the NO 2 remover mentioned above, which has excellent performance in the presence of water vapor.
By sandwiching the oxidation catalyst and creating a sandwich structure,
Moisture in the air easily accumulates between the polypropylene nonwoven fabric, NO 2 removal agent, and CO oxidation catalyst, greatly improving performance.
以上のフイルター構造によつて、従来から待望
されていたフアン付暖房機による室内空気汚染の
防止がほゞ完全に達成できる。 With the above filter structure, it is possible to almost completely achieve the long-awaited prevention of indoor air pollution caused by fan-equipped heaters.
第1図は本発明の実施例におけるフアン付暖房
機の概略説明図、第2図はNO2除去剤の特性を示
す図、第3図はCO酸化触媒の特性を示す図であ
る。
1……有害ガス除去フイルター、2……温風吹
出フアン、3……燃焼器。
FIG. 1 is a schematic explanatory diagram of a fan-equipped heater according to an embodiment of the present invention, FIG. 2 is a diagram showing the characteristics of the NO 2 removing agent, and FIG. 3 is a diagram showing the characteristics of the CO oxidation catalyst. 1...Harmful gas removal filter, 2...Hot air blowing fan, 3...Combustor.
Claims (1)
空気流路に、ポリプロピレン不織布ではさんでサ
ンドイツチ構成にした有害ガス除去フイルターと
してアルカリとセメント材と粉末活性炭の混練成
型物よりなるNO2除去剤、及びアルカリ・セメン
ト材と粉末活性炭との混練成型物に貴金属触媒を
担持させたCO酸化触媒を単独あるいは同時に設
置したことを特徴とするフアン付暖房機。 2 前記有害ガス除去フイルターが、暖房機の空
気吸い込み口に設置されている特許請求の範囲第
1項記載のフアン付暖房機。 3 前記有害ガス除去フイルターとしてのNO2除
去剤が、アルカリとして炭酸カリウムと水酸化カ
ルシウムを、セメント材として焼石こうをそれぞ
れ用いた特許請求の範囲第1項記載のフアン付暖
房機。 4 前記有害ガス除去フイルターとしてのCO酸
化触媒体が、アルカリとして炭酸カリウムを、セ
メント材としてアルミン酸石灰をそれぞれ用い、
貴金属触媒として白金とパラジウムを同時に担持
させた特許請求の範囲第1項記載のフアン付暖房
機。[Scope of Claims] 1. A kneaded molded product of alkali, cement material, and powdered activated carbon as a harmful gas removal filter sandwiched between polypropylene nonwoven fabrics and configured as a sandwich sandwich in the air flow path of a heater with a built-in combustor and hot air blowing fan. A heating machine with a fan, characterized in that a NO 2 removing agent consisting of the above, and a CO oxidation catalyst in which a precious metal catalyst is supported on a kneaded molded product of an alkali cement material and powdered activated carbon are installed singly or simultaneously. 2. The fan-equipped heater according to claim 1, wherein the harmful gas removal filter is installed at an air intake port of the heater. 3. The fan-equipped heater according to claim 1, wherein the NO 2 removing agent as the harmful gas removing filter uses potassium carbonate and calcium hydroxide as the alkali and calcined gypsum as the cement material. 4. The CO oxidation catalyst as the harmful gas removal filter uses potassium carbonate as the alkali and lime aluminate as the cement material,
A fan-equipped heater according to claim 1, in which platinum and palladium are simultaneously supported as noble metal catalysts.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14459479A JPS5667528A (en) | 1979-11-07 | 1979-11-07 | Heater with fan |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14459479A JPS5667528A (en) | 1979-11-07 | 1979-11-07 | Heater with fan |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5667528A JPS5667528A (en) | 1981-06-06 |
| JPS6152732B2 true JPS6152732B2 (en) | 1986-11-14 |
Family
ID=15365689
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14459479A Granted JPS5667528A (en) | 1979-11-07 | 1979-11-07 | Heater with fan |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5667528A (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS53115687A (en) * | 1977-03-18 | 1978-10-09 | Matsushita Electric Ind Co Ltd | Gas purifying catalytic member |
| JPS6025177B2 (en) * | 1977-04-20 | 1985-06-17 | 松下電器産業株式会社 | gas purification equipment |
-
1979
- 1979-11-07 JP JP14459479A patent/JPS5667528A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5667528A (en) | 1981-06-06 |
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