JPH02159203A - Catalyzer combustion apparatus - Google Patents

Catalyzer combustion apparatus

Info

Publication number
JPH02159203A
JPH02159203A JP31406088A JP31406088A JPH02159203A JP H02159203 A JPH02159203 A JP H02159203A JP 31406088 A JP31406088 A JP 31406088A JP 31406088 A JP31406088 A JP 31406088A JP H02159203 A JPH02159203 A JP H02159203A
Authority
JP
Japan
Prior art keywords
gas
tank
temperature
catalyzer
lowered
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
Application number
JP31406088A
Other languages
Japanese (ja)
Inventor
Haruo Ida
治夫 井田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP31406088A priority Critical patent/JPH02159203A/en
Publication of JPH02159203A publication Critical patent/JPH02159203A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To discharge much gas at the time of initial rise and discharge an only a gas quantity necessary for keeping a constant temperature after temperature rise by a method wherein gas gasified by a carburetor is throttled with a nozzle to jet the gas at a high speed, wherein the gas is mixed with air, wherein an injector section for feeding the gas to a catalyzer is set to burn the catalyzer, and wherein the interior of a tank is composed of thermal insulation materials. CONSTITUTION:By a resistor 31, the current of gas is limited, and the gas is jetted at a high speed from a jet port 34 at the tip of a nozzle 33, and ambient air is sucked up by an injector section 35, and the mixture of proper gas and air is made and is fed to a catalyzer 40. The catalyzer is fired by a firing device 41, and catalyzer combustion is started. A tank 39 forms a thermal insulation structure as a whole by jointing the thermal insulation materials 38 to the internal surface of the tank. When gas is started to come out, then by the vapor heat of the gas, the temperature of liquefied gas in the tank is lowered, and so in an initial state, a temperature in the tank is equal to a room temperature, and tank internal-pressure is high, and so an initial gas flow rate is high, but by the vapor heat of the gas, the temperature in the tank is lowered, and accordingly, the internal pressure is lowered, and a gas flow rate is lowered.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は液化石油ガスを用いた一般家庭用の触媒燃焼装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a catalytic combustion device for general household use using liquefied petroleum gas.

従来の技術 従来、この種の触媒燃焼装置は第3.4図に示すような
構造であった。この第3,4図はへアーカーラーの例で
あって、1は抵抗体で、タンク2の圧力で流出する液化
ガスの量を一定量に押える働きをする。一定量におさえ
られた液化ガスは周囲より熱を受けて気化する。すなわ
ち、この抵抗体1が液化ガスの気化装置そのものである
。気化したガスは弁部3とノズル4を通って約e○μm
の微小孔5かも噴出し、インジェクタ一部の孔10で周
囲から空気を巻き込み、触媒8に供給する。
Prior Art Conventionally, this type of catalytic combustion apparatus has had a structure as shown in FIG. 3.4. Figures 3 and 4 show examples of hair curlers, and 1 is a resistor which functions to suppress the amount of liquefied gas flowing out under the pressure of a tank 2 to a constant amount. The liquefied gas, which is held in a certain amount, receives heat from its surroundings and vaporizes. That is, this resistor 1 is the liquefied gas vaporization device itself. The vaporized gas passes through the valve part 3 and nozzle 4 and has a thickness of approximately e○μm.
The small holes 5 of the injector also eject air, and air is drawn in from the surrounding area through the holes 10 of a part of the injector and supplied to the catalyst 8.

6および7は2本の熱膨張率の異るパイプで、このパイ
プの外側に取付けた触媒8の燃焼熱を受け、この2本の
バイブロ、7の熱膨張の差によりノズル4の弁部3を開
閉して燃焼温度を制御している。
6 and 7 are two pipes with different coefficients of thermal expansion, and receive the combustion heat of the catalyst 8 installed on the outside of these pipes. The combustion temperature is controlled by opening and closing.

9は灯芯、11は点火装置である。この種の燃焼装置に
制御機構を用いている理由は、主として加熱部をできる
だけ早く加熱して、一定の温度にするためであり、点火
直後の立上り時は大量のガスを消費し、温度が飽和して
くるとガスの量を絞る制御をおこなっている。
9 is a lamp wick, and 11 is an ignition device. The reason why a control mechanism is used in this type of combustion device is to heat the heating part as quickly as possible and keep it at a constant temperature. When this happens, a control is performed to reduce the amount of gas.

発明が解決しようとする課題 従来の構成では温度制御をおこなうための複雑な機構が
必要であるが、実用面から考えると、立上り時に多電の
ガスを出し、飽和温度に近ずくと飽和温度を維持するの
に必要な量のガスを出すという2段階のガス量を出す機
構があれば、従来の温度制御機構の代替が可能となる。
Problems to be Solved by the Invention Conventional configurations require a complicated mechanism for temperature control, but from a practical perspective, a high-voltage gas is emitted at startup, and when the temperature approaches the saturation temperature, the saturation temperature is lowered. If there is a mechanism that outputs the amount of gas in two stages to output the amount of gas necessary to maintain the temperature, it will be possible to replace the conventional temperature control mechanism.

本発明は初期の立上シ時には多量のガスを放出し、昇温
後は一定の温度を保つのに必要なガス量のみを放出する
ガス供給装置を持った触媒燃焼装置を提供するものであ
る。
The present invention provides a catalytic combustion device that has a gas supply device that releases a large amount of gas during initial start-up and only releases the amount of gas necessary to maintain a constant temperature after temperature rise. .

課題を解決するための手段 本発明の燃焼装置は、液化石油ガスを貯蔵するタンク部
と液化石油ガスの流量を制限して気化させる気化装置と
、この気化装置で気化したガスをノズルで絞って、高速
で噴出させ、空気と混合して、触媒に供給するインジェ
クタ部とを設けて触媒燃焼させるように構成すると共に
、前記タンクの内部を、断熱材で構成したものである。
Means for Solving the Problems The combustion device of the present invention comprises a tank section for storing liquefied petroleum gas, a vaporizer for vaporizing the liquefied petroleum gas by limiting the flow rate of the liquefied petroleum gas, and a nozzle for squeezing the gas vaporized by the vaporizer. The fuel tank is configured to include an injector section that ejects the fuel at high speed, mixes it with air, and supplies the mixture to the catalyst for catalytic combustion, and the interior of the tank is constructed of a heat insulating material.

作用 この構成によると、スイッチを入れてガスが出しはじめ
ると、ガスの蒸発熱で、タンク内の液化ガスの温度が低
下していくため、初期状態では、タンクの内部の温度が
室温に等しく、タンク内圧が高いため、初期のガス流量
は多いが、ガスの蒸発熱によりタンク内の温度が低下し
、そのため内圧が低下し、ガス流量が少なくなるのであ
る。
Effects According to this configuration, when the switch is turned on and gas starts to flow out, the temperature of the liquefied gas in the tank decreases due to the heat of evaporation of the gas, so that in the initial state, the temperature inside the tank is equal to room temperature. Since the tank internal pressure is high, the initial gas flow rate is high, but the temperature inside the tank decreases due to the heat of evaporation of the gas, which causes the internal pressure to decrease and the gas flow rate to decrease.

実施例 以下その実施例を第1図及び第2図を参照して説明する
EXAMPLES The following examples will be described with reference to FIGS. 1 and 2.

図において、31は抵抗体でガスの流れを制限するもの
である。32は弁部、33はノズルで、ガスはこのノズ
ル33の先端の噴出口34より高速で、賞出する。噴出
したガスはインジェクタ部36で周囲の空気を吹い込み
、適切なガスと空気の混合気を作り触媒4oに供給する
。そして着火装置41により着火され、触媒燃焼が開始
する。また灯芯36を介して抵抗体31に液化燃料37
を供給するタンク39は、その内面に断熱材38を接合
して全体として断熱構成を採っている。ところでノズル
33から出るガスの流量は、タンク39の内圧に比例す
る。タンク39の内圧はタンク内の液化石油ガスの温度
に比例する。今、イソブタンの蒸発潜熱は、91.6i
 CILl/fであシ、比熱は0.229 tml/f
℃である。仮に、初期段階で0.51のガスが蒸発し、
タンク39内にガスが6g残っていて、蒸発潜熱の半分
がガスの冷却に使われたとすると、約20℃の温度の低
下がある計算となる。その場合、圧力は、初期が室温と
同じ20℃とするならばO’Cとなり、内圧はゲージ圧
で2.2 kg/cg →o、e kg/an−となり
1/3.7に減少する。
In the figure, 31 is a resistor that restricts the flow of gas. 32 is a valve portion, 33 is a nozzle, and gas is ejected at a higher speed than a jet port 34 at the tip of this nozzle 33. The ejected gas is injected with surrounding air by the injector section 36 to create an appropriate mixture of gas and air, which is then supplied to the catalyst 4o. Then, it is ignited by the ignition device 41, and catalytic combustion starts. In addition, the liquefied fuel 37 is connected to the resistor 31 via the lamp wick 36.
The tank 39 for supplying the water has a heat insulating structure as a whole by bonding a heat insulating material 38 to its inner surface. Incidentally, the flow rate of gas coming out of the nozzle 33 is proportional to the internal pressure of the tank 39. The internal pressure of the tank 39 is proportional to the temperature of the liquefied petroleum gas within the tank. Now, the latent heat of vaporization of isobutane is 91.6i
CILl/f, specific heat is 0.229 tml/f
It is ℃. If 0.51 of the gas evaporates in the initial stage,
If 6 g of gas remains in the tank 39 and half of the latent heat of vaporization is used to cool the gas, it is calculated that the temperature will decrease by about 20°C. In that case, if the initial pressure is 20℃, which is the same as room temperature, the pressure will be O'C, and the internal pressure will be 2.2 kg/cg in gauge pressure → o, e kg/an-, which will decrease to 1/3.7. .

従がって、ガス流量も1/3.7になるわけである。Therefore, the gas flow rate is also reduced to 1/3.7.

実際は、温度の低下により、流量低下→蒸発熱の減少と
いう過程をとるため、これほど急激な低下はせず、初期
と飽和時の流量差は捧程度になる。
In reality, as the temperature decreases, the flow rate decreases and the heat of vaporization decreases, so the decrease is not as rapid as this, and the difference in flow rate between the initial stage and the saturated stage is only about the same.

又これはタンク39の断熱の状態により変わる。This also changes depending on the state of insulation of the tank 39.

このようにして、ガス貯蔵タンク39を断熱することに
より、ガスの蒸発潜熱を利用して、初期の昇温時にガス
流量を多く、飽和時に少なくする構造を得ることができ
る。
By insulating the gas storage tank 39 in this manner, it is possible to obtain a structure in which the gas flow rate is increased during initial temperature rise and decreased during saturation by utilizing the latent heat of vaporization of the gas.

発明の効果 このように本発明は、タンクを断熱構成としたことによ
り、初期に多量のガスを流し、従って、急激に温度が立
上り、飽和状態に近づくと適当なガス流量を得ることが
できるようになる。この装置があれば、温度によりガス
流量を制御する複雑な機構が必要でなくなり、簡便な触
媒燃焼装置を得ることができる。
Effects of the Invention As described above, the present invention has an insulated structure for the tank, which allows a large amount of gas to flow at the beginning, so that when the temperature rises rapidly and approaches saturation, an appropriate gas flow rate can be obtained. become. With this device, a complicated mechanism for controlling gas flow rate based on temperature is no longer necessary, and a simple catalytic combustion device can be obtained.

なお、上記した実施例ではタンクの内面に断熱性を得る
ための部材(例えば発泡グラスチック等)を接合した例
を述べたが、このほかタンクそのものを断熱性材料で構
成することも考えられる。
In addition, in the above-mentioned embodiment, an example was described in which a member (for example, foamed plastic, etc.) for obtaining heat insulation properties was bonded to the inner surface of the tank, but it is also possible to construct the tank itself from a heat insulation material.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の実施例を示す触媒燃焼装置の要部拡大
断面図、第2図は全体断面図、第3図は従来の触媒燃焼
式へアーカーラーの断面図、第4図は第3図の要部拡大
断面図であるみ 31・・・・・・気化装置(抵抗体)、33・・・・・
・ノズル、35・・・・・・インジェ・フタ部、39・
・・・・・タンク。 代理人の氏名 弁理士 粟 野 重 孝 ほか1名第 図 35−一〜イ」じエクタ甚V
Fig. 1 is an enlarged sectional view of the main parts of a catalytic combustion device showing an embodiment of the present invention, Fig. 2 is an overall sectional view, Fig. 3 is a sectional view of a conventional catalytic combustion type curler, and Fig. 4 is a sectional view of a conventional catalytic combustion type curler. This is an enlarged cross-sectional view of the main parts of Figure 3. 31... Vaporization device (resistor), 33...
・Nozzle, 35...Injector lid part, 39・
·····tank. Name of agent: Patent attorney Shigetaka Awano and one other person

Claims (1)

【特許請求の範囲】[Claims] 液化石油ガスの流量を制限して気化させる気化装置と、
この気化装置で気化したガスをノズルで絞って高速で噴
出させ、空気と混合して触媒に供給するインジェクタ部
とを具備し、上記液化石油ガスを貯蔵するタンクは断熱
構造部材で構成した触媒燃焼装置。
a vaporizer that limits the flow rate of liquefied petroleum gas and vaporizes it;
The gas vaporizer is equipped with an injector section that squeezes the vaporized gas through a nozzle to eject it at high speed, mixes it with air, and supplies it to the catalyst. Device.
JP31406088A 1988-12-13 1988-12-13 Catalyzer combustion apparatus Pending JPH02159203A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31406088A JPH02159203A (en) 1988-12-13 1988-12-13 Catalyzer combustion apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31406088A JPH02159203A (en) 1988-12-13 1988-12-13 Catalyzer combustion apparatus

Publications (1)

Publication Number Publication Date
JPH02159203A true JPH02159203A (en) 1990-06-19

Family

ID=18048742

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31406088A Pending JPH02159203A (en) 1988-12-13 1988-12-13 Catalyzer combustion apparatus

Country Status (1)

Country Link
JP (1) JPH02159203A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003534862A (en) * 2000-06-03 2003-11-25 ブラウン ゲーエムベーハー Catalytic gas combustion device for appliances for personal use

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003534862A (en) * 2000-06-03 2003-11-25 ブラウン ゲーエムベーハー Catalytic gas combustion device for appliances for personal use

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