CN207936532U - A kind of water, gas thermal response catalyst oven - Google Patents
A kind of water, gas thermal response catalyst oven Download PDFInfo
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- CN207936532U CN207936532U CN201820107673.0U CN201820107673U CN207936532U CN 207936532 U CN207936532 U CN 207936532U CN 201820107673 U CN201820107673 U CN 201820107673U CN 207936532 U CN207936532 U CN 207936532U
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- reacting furnace
- heating tube
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Abstract
A kind of water of the utility model offer, gas thermal response catalyst oven, include reacting furnace, multiple catalyst reactants, fuel apparatus and air-extractor：Heating tube is equipped in reacting furnace, multiple catalyst reactants are set in heating tube, and reacting furnace is equipped with hot air discharge mouth, water inlet pipe and outlet pipe；Fuel apparatus connects to be formed with heating tube；Air-extractor connects to be formed with reacting furnace；Whereby, by in fuel apparatus conveying fuel to heating tube, so that multiple catalyst reactants and fuel is formed thermal response and persistently generates thermal energy and heating tube is heated, it is conveyed in a liquid to reacting furnace by water inlet pipe, liquid is heated by heating tube, makes the liquid heated that can be flowed out by outlet pipe；In addition, the hot gas in reacting furnace can be delivered to the interior space by air-extractor, reaches and be not required to carry out air heating with combustion system, generated carbonized particles when avoiding burning, so as to being effectively improved air quality.
Description
Technical field
It is the utility model is related to a kind of water, gas thermal response catalyst oven, more particularly to a kind of in anti-using heat in a reacting furnace
Mode is answered, the thermal response of a duration is generated, and using the thermal energy of duration produced by the thermal response, with to adding in reacting furnace
Heat pipe is heated, and is then exhausted from after being heated to the liquid in reacting furnace by heating tube and is used with supplying hot water；In addition, reacting furnace
Interior hot gas also can be delivered to the interior space by air-extractor so that effectively promote interior space temperature；Meanwhile reaching and being not required to
Air heating is carried out in a manner of traditional combustion, generated carbonized particles when avoiding burning, so as to being effectively improved air quality.
Background technology
Currently, due to terrestrial climate transition, global temperatures generate the extreme climates such as extremely cold and very hot, many subtropical zones
Never snowy area also in recent years down snowstorm, original warming equipment has not been inconsistent use；Therefore, work as cold snap,
Indoor temperature rapid drawdown, in order to resist severe cold, the far infrareds such as hand warmer, electric heater are more favored by consumer.
Traditional large-scale heating equipment is to need to burn a large amount of coal to manufacture thermal energy, and in combustion process, can not be excluded
Generated a large amount of carbonized particles are then to cause air pollution arch-criminal, so that the thin suspended particulates in air（PM2.5, directly
Jing≤2.5 micron）It is continuous to increase.
In addition to this, using thermal energy caused by combustion system, other than it will produce thin suspended particulates, still there are many lack
It falls into；Such as：The presence of open fire danger is had as long as using combustion system, and seriously threatening property is caused to life and property；Moreover,
If heating equipment manufactures thermal energy with combustion system, it can to generate pressure because of burning inside heating equipment；Once pressure
It is not affected by control, then will produce volatile danger.
Therefore, how to research and develop one kind being not required to that with combustion system thermal energy can be generated, and the heating that can heat liquid is set
It is standby, as the utility model major subjects to be solved.
Utility model content
According to water disclosed in the utility model, gas thermal response catalyst oven, include reacting furnace, multiple catalyst reactants,
Fuel apparatus and air-extractor：Reacting furnace is internally provided with a reative cell, and a heating tube, the outside of reacting furnace are equipped in reative cell
It is additionally provided with the first tube body, is connected by one end of the first tube body and the outlet side of heating tube, one is equipped with by the other end of the first tube body
Current divider, and current divider is connected with waste gas pipeline and air delivery pipe and is respectively connected to the inlet end of heating tube, and it is anti-
Answer stove to be additionally provided with a hot air discharge mouth, a water inlet pipe, an outlet pipe and a heater, heater be disposed adjacent in heating tube into
Gas end；Multiple catalyst reactants are set in heating tube, and catalyst reactant is tool metal component；Fuel apparatus is connected with reacting furnace
It connects comprising have a propellant bottle and a petrolift, and be connected with petrolift with propellant bottle, then be connected with heating tube by petrolift
It connects, a fuel is stored in propellant bottle；Air-extractor is connected with reacting furnace, by the hot air discharge mouth phase of air-extractor and reacting furnace
Connection, and air-extractor is additionally provided with a gas outlet.
The technical characteristics of the utility model is, using thermal response is carried out in reacting furnace, to generate the thermal energy of a duration,
First catalyst reactant is heated by heater, then is conveyed the fuel in propellant bottle via third tube body by petrolift
To the heating tube of reacting furnace, catalyst reactant is made to form thermal response with fuel and persistently generate thermal energy and add to heating tube
Heat；In addition, again by water inlet pipe conveying one liquid to the reative cell of reacting furnace, being heated to liquid by heating tube, making to have added
The liquid of heat can be flowed out by outlet pipe, to be provided as hot water use；Moreover, reacting gas outlet of the indoor hot gas by air-extractor
It is delivered to the interior space, to be provided as heating use；Furthermore the thermal energy that these catalyst reactants generate after thermal response, via
First tube body, current divider and the waste gas pipeline are back in heating tube again, and by current divider and air delivery pipe conveying
In extraneous air to the heating tube.Therefore, the reacting furnace for reaching the utility model is not required to, with combustion system, carry out air and liquid
Heating, generated carbonized particles when avoiding burning, so as to being effectively improved air quality.
Preferably, gas thermal response catalyst oven, the reacting furnace are further provided with a control panel, the control panel respectively with this
Heater and the petrolift are electrically connected.
Preferably, the catalyst reactant has at least one above metal component.
Preferably, the catalyst reactant is equipped at least one perforation.
Preferably, the fuel can be methanol, ethyl alcohol, isopropyl alkali, methane one of which.
Preferably, top position of the outlet side adjacent to the reacting furnace, bottom of the inlet end adjacent to the reacting furnace
Position.
Preferably, top position of the hot air discharge mouth adjacent to the reacting furnace.
Description of the drawings
Fig. 1 is the utility model water, one Application Example schematic diagram of gas thermal response catalyst oven.
Fig. 2 is the one reagentia schematic diagram of explanation of the utility model heating reaction furnace.
Fig. 3 is the reaction heated condition schematic diagram of the utility model heating reaction furnace.
Fig. 4 is another embodiment schematic diagram of catalyst reactant of the utility model heating reaction furnace.
Reference sign
1, reacting furnace
10, reative cell
11, heating tube
111, outlet side
112, inlet end
12, the first tube body
121, current divider
122, waste gas pipeline
123, air delivery pipe
13, hot air discharge mouth
14, water inlet pipe
15, outlet pipe
16, heater
17, control panel
2, catalyst reactant
21, it perforates
3, fuel apparatus
31, propellant bottle
32, petrolift
33, the second tube body
34, third tube body
4, air-extractor
41, the 4th tube body
42, gas outlet
5, liquid
6, the interior space.
Specific implementation mode
To the technical solution of the utility model and advantageous effect there is further understanding, now coordinates the utility model
Attached drawing describes the feature and advantage of the utility model in detail, and the viewpoint of the utility model is further described in embodiment below,
But it is non-anyways to limit the scope of protection of the utility model.
It please refers to Fig.1, shown in 2,3,4, the utility model discloses a kind of water, gas thermal response catalyst ovens, include one anti-
Answer stove 1, multiple catalyst reactants 2, a fuel apparatus 3 and an air-extractor 4.
Reacting furnace 1 is internally provided with a reative cell 10, is equipped with a heating tube 11 in reative cell 10, one end of heating tube 11 is set
There are an outlet side 111 and its other end to be equipped with an inlet end 112, and the outlet side 111 of heating tube 11 can be adjacent to reacting furnace 1
Top position, and the inlet end 112 of heating tube 11 can be adjacent to the bottom position of reacting furnace 1, and the outside of reacting furnace 1 is additionally provided with
One first tube body 12 is connect by one end of the first tube body 12 with the outlet side 111 of heating tube 11, by the other end of the first tube body 12
Equipped with a current divider 121, and current divider 121 is connected with a waste gas pipeline 122 and an air delivery pipe 123, exhaust gas conveying
Pipe 122 and air delivery pipe 123 are respectively connected to the inlet end 112 of heating tube 11 again；Moreover, reacting furnace 1 is additionally provided with a hot gas
Floss hole 13, a water inlet pipe 14, an outlet pipe 15, a heater 16 and a control panel 17, heater 16 are disposed adjacent in adding
The inlet end 112 of heat pipe 11, to be heated to multiple catalyst reactants 2 in heating tube 11；The heater 16 and control
Panel 17 processed is electrically connected, and is controlled the startup of heater 16 by control panel 17 or is closed；The hot air discharge mouth 13 can be adjacent to
The top position of reacting furnace 1, the water inlet pipe 14 and outlet pipe 15 are communicated with the formation of the reative cell of reacting furnace 1 10 respectively, and into
The other end of water pipe 14 and outlet pipe 15 may extend to an interior space 6.
For multiple catalyst reactants 2 to be set in the heating tube 11 of reacting furnace 1, catalyst reactant 2 has at least two kinds
Above metal component, such as：Catalyst reactant 2 can be at least two or more metal object institute groups such as copper, zinc, silver, iron
At；And catalyst reactant 2 is equipped at least one perforation 21 so that catalyst reactant 2 has good gas by set perforation 21
Flow through permeability.
Fuel apparatus 3 to be connected with reacting furnace 1, the fuel apparatus 3 its include a propellant bottle 31 and a fuel
Pump 32, is connected with one second tube body 33, and the other end of petrolift 32 is connected with a third between propellant bottle 31 and petrolift 32
Tube body 34, is connected to the first tube body 12 of reacting furnace 1 by the other end of third tube body 34, and third tube body 34 and the first tube body 12
112 position of inlet end for the place then adjacent heating tube 11 that is connected, and storing a fuel, the fuel inside propellant bottle 31
Can be the fuel such as methanol, ethyl alcohol, isopropyl alkali, methane.
For air-extractor 4 to be connected with reacting furnace 1, the air-extractor 4 is connected with one the 4th tube body 41, by the 4th pipe
The other end of body 41 is connected to the hot air discharge mouth 13 of reacting furnace 1, and air-extractor 4 is additionally provided with a gas outlet 42, gas outlet 42
It may be disposed in an interior space 6；4 inside of the air-extractor can be equipped with extraction fan.
When the petrolift 32 of the fuel apparatus 3 starts, stored fuel is flowed through by the second tube body 33 in propellant bottle 31
Petrolift 32, then it is delivered to by third tube body 34 and the first tube body 12 inlet end 112 of heating tube 11, make fuel that can be touched with multiple
Matchmaker's reactant 2 forms thermal response and persistently generates thermal energy and heated to heating tube 11；Thermal energy inside heating tube 11 at this time,
It can be discharged by outlet side 111, via the first tube body 12 and current divider 121, catalyst reactant 2 is formed by heat through thermal response at this time
Can, it can be back to again in heating tube 11 by waste gas pipeline 122 again, and can be by extraneous air via air by current divider 121
Delivery pipe 123 is sent to heating tube 11, to provide oxygen of the catalyst reactant 2 needed for thermal response.
The water inlet pipe 14 can be by outside liquid（Such as：Water）It is delivered in the reative cell 10 of reacting furnace 1, then by outlet pipe 15
Liquid in the reative cell 10 of reacting furnace 1 can be discharged.
The utility model attempts an embodiment, when reacting furnace 1 starts, first by heater 16 by multiple catalyst reactants 2
It is heated（Such as：00100 DEG C of heating temperature ＞）, when catalyst reactant 2 reaches a heating temperature, then by fuel apparatus 3
Petrolift 32 delivers fuel to the inlet end 112 of heating tube 11 so that fuel can form thermal response with multiple catalyst reactants 2
And continue to generate and thermal energy and heating tube 11 be heated, heater 16 can then close at this time, without again to catalyst reactant 2 into
Row heating；In addition, by water inlet pipe 14 convey liquid to the reative cell 10 of reacting furnace 1 in, you can by heating tube 11 to liquid into
Row heating, and being heated liquid then can be flowed out by outlet pipe 15, to be provided as hot water use；Meanwhile the reaction of reacting furnace 1
10 internal cause heating tube 11 of room is with thermal energy caused by thermal response（Hot gas）It can be extracted out by air-extractor 4, i.e. heat in reative cell 10
Air-extractor 4 can be delivered to through the 4th tube body 41 by hot air discharge mouth 13, then by air-extractor 4 gas outlet 42 by thermal energy
（Hot gas）It is delivered to the interior space 6, to be provided as warmer use so that effectively promote interior space temperature.
Noticeable thing, the thermal energy that multiple catalyst reactants 2 generate after thermal response, can via the first tube body 12, point
The thermal energy not being fully utilized is back in heating tube 11 by stream device 121 and waste gas pipeline 122 to be recycled, and by current divider 121
And air delivery pipe 123 is conveying in extraneous air to heating tube 11.Moreover, the control panel 17 can with heater 16,
Petrolift 32 is electrically connected, when reacting furnace 1 is in running, by control panel 17 to monitor the temperature of reacting furnace 1, by controlling
Panel 14 carries out heater 16, petrolift 32 according to the temperature information of acquiescence the control of stopping or intermittent start.
The technical characteristics of the utility model is, can be formed with fuel using multiple catalyst reactants 2 in reacting furnace 1 hot anti-
Thermal energy is answered and persistently generates, and multiple catalyst reactants 2 only can give off carbon dioxide and water with during fuel reaction, because
This reacting furnace 1 in being not required to be heated with combustion system using process completely, generated carbonized particles when avoiding burning, so as to
It is effectively improved air quality, while not having the danger of open fire and generating the danger of pressure explosion because of burning.
Claims (6)
1. a kind of water, gas thermal response catalyst oven, which is characterized in that include：
One reacting furnace is internally provided with a reative cell, is equipped with a heating tube in the reative cell, one end of the heating tube goes out equipped with one
Gas end and its other end are equipped with an inlet end, and the outside of the reacting furnace is additionally provided with one first tube body, one end of first tube body with
The outlet side connects and its other end is equipped with a current divider, which is connected with a waste gas pipeline and an air delivery
Pipe, the waste gas pipeline and the air delivery pipe are respectively connected to the inlet end of the heating tube, and the reacting furnace is additionally provided with a heat
Gas floss hole, a water inlet pipe, an outlet pipe and a heater, the heater are disposed adjacent the inlet end in the heating tube；
Multiple catalyst reactants are set in the heating tube of the reacting furnace；
Fuel apparatus is connected with the reacting furnace, which includes a propellant bottle and a petrolift, the propellant bottle with should
One second tube body is connected between petrolift, one end of the petrolift is connected with a third tube body, and one end of the third tube body connects
It is connected to the first tube body of the reacting furnace, a fuel is stored by the propellant bottle；
One air-extractor is connected with the reacting furnace, which is connected with one the 4th tube body, and one end of the 4th tube body connects
It is connected to the hot air discharge mouth of the reacting furnace, which is additionally provided with a gas outlet；
The water inlet pipe, the outlet pipe and the gas outlet each extend in an interior space, are first touched these by the heater
Matchmaker's reactant heats, then the fuel in the propellant bottle is delivered to the reacting furnace by the third tube body by the petrolift
In heating tube, these catalyst reactants is made to form thermal response with the fuel and persistently generate thermal energy and add to the heating tube
Heat, then by water inlet pipe conveying one liquid to the reative cell of the reacting furnace, being heated, being made to the liquid by the heating tube
The liquid of heating is flowed out by the outlet pipe, and the indoor hot gas of the reaction is delivered to the room by the gas outlet of the air-extractor
Interior space, the thermal energy that these catalyst reactants generate after thermal response are conveyed by first tube body, the current divider and the exhaust gas
Pipe is back to again in the heating tube, and by the current divider and the air delivery pipe conveying in extraneous air to the heating tube.
2. water as described in claim 1, gas thermal response catalyst oven, which is characterized in that the reacting furnace is further provided with a control
Panel, the control panel are electrically connected with the heater and the petrolift respectively.
3. water as described in claim 1, gas thermal response catalyst oven, which is characterized in that the catalyst reactant is worn equipped at least one
Hole.
4. water as described in claim 1, gas thermal response catalyst oven, which is characterized in that the fuel can be methanol, ethyl alcohol, different
Third alkali, methane one of which.
5. water as described in claim 1, gas thermal response catalyst oven, which is characterized in that the outlet side is adjacent to the reacting furnace
Top position, bottom position of the inlet end adjacent to the reacting furnace.
6. water as described in claim 1, gas thermal response catalyst oven, which is characterized in that the hot air discharge mouth is adjacent to the reaction
The top position of stove.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820107673.0U CN207936532U (en) | 2018-01-23 | 2018-01-23 | A kind of water, gas thermal response catalyst oven |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820107673.0U CN207936532U (en) | 2018-01-23 | 2018-01-23 | A kind of water, gas thermal response catalyst oven |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207936532U true CN207936532U (en) | 2018-10-02 |
Family
ID=63649913
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820107673.0U Active CN207936532U (en) | 2018-01-23 | 2018-01-23 | A kind of water, gas thermal response catalyst oven |
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| Country | Link |
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| CN (1) | CN207936532U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111238028A (en) * | 2018-11-28 | 2020-06-05 | 台湾时代能量股份有限公司 | Chemical energy heat conversion reaction furnace, air conditioner control system and liquid heating control system |
| CN113446652A (en) * | 2021-06-24 | 2021-09-28 | 北京科技大学 | Emergency heating device and method based on self-heating material |
-
2018
- 2018-01-23 CN CN201820107673.0U patent/CN207936532U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111238028A (en) * | 2018-11-28 | 2020-06-05 | 台湾时代能量股份有限公司 | Chemical energy heat conversion reaction furnace, air conditioner control system and liquid heating control system |
| CN113446652A (en) * | 2021-06-24 | 2021-09-28 | 北京科技大学 | Emergency heating device and method based on self-heating material |
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