CN213631036U - Diversified heat exchange reactor without open fire - Google Patents
Diversified heat exchange reactor without open fire Download PDFInfo
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- CN213631036U CN213631036U CN202022413162.1U CN202022413162U CN213631036U CN 213631036 U CN213631036 U CN 213631036U CN 202022413162 U CN202022413162 U CN 202022413162U CN 213631036 U CN213631036 U CN 213631036U
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Abstract
The utility model provides a no open fire pluralism heat replacement reactor, including barrel, support, the barrel is established on the support, be equipped with heat exchange tube, baffle and methyl alcohol oxidation catalyst in the barrel, methyl alcohol oxidation catalyst surface cladding has rare earth metal, the one end lateral wall of barrel is equipped with the air-supply line, advances oil pipe, goes out the tuber pipe, the front end that advances oil pipe stretches into in the air-supply line, play tuber pipe are located respectively the both sides of baffle, the bottom of barrel, top be equipped with respectively with inlet tube, the outlet pipe of the both ends intercommunication of heat exchange tube, the bottom of barrel is the blow off pipe in addition. The design does not need open fire, realizes zero emission, has the functions of replacing hot water, hot air and steam, and has the advantages of small volume, quick heating and high safety; can replace the traditional boiler and is the best substitute of the oil-fired boiler in the current market.
Description
Technical Field
The utility model relates to a heat exchanger technical field specifically is no open fire pluralism heat exchange reactor.
Background
At present, most of domestic bath hot water is supplied by a solar water heater or a gas water heater, the solar water heater does not need to supply power or burn gas, but the solar water heater generates heat slowly and is easily influenced by weather; gas water heaters require the combustion of gas and can create safety hazards if the combustion is incomplete.
SUMMERY OF THE UTILITY MODEL
In view of the technical deficiencies, the utility model aims to provide a diversified heat exchange reactor without open flame.
In order to solve the technical problem, the utility model adopts the following technical scheme:
the utility model provides a no open fire pluralism heat replacement reactor, including barrel, support, the barrel is established on the support, be equipped with heat exchange tube, baffle and methyl alcohol oxidation catalyst in the barrel, methyl alcohol oxidation catalyst surface cladding has rare earth metal, the one end lateral wall of barrel is equipped with the air-supply line, advances oil pipe, goes out the tuber pipe, the front end that advances oil pipe stretches into in the air-supply line, play tuber pipe are located respectively the both sides of baffle, the bottom of barrel, top be equipped with respectively with inlet tube, the outlet pipe of the both ends intercommunication of heat exchange tube, the bottom of barrel is the blow off pipe in addition.
Preferably, the methanol oxidation catalyst is filled in the cylinder.
The beneficial effects of the utility model reside in that: the design does not need open fire, realizes zero emission, has the functions of replacing hot water, hot air and steam, and has the advantages of small volume, quick heating and high safety; can replace the traditional boiler and is the best substitute of the boiler using fuel oil (particle, diesel oil, heavy oil and coal) in the current market.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
Fig. 1 is a schematic structural diagram (a transparent shell schematic diagram) of a multiplex heat exchange reactor without an open flame according to an embodiment of the present invention.
Description of reference numerals:
1-cylinder, 2-bracket, 3-heat exchange tube, 4-clapboard, 5-methanol oxidation catalyst, 6-air inlet tube, 7-oil inlet tube, 8-air outlet tube, 9-water inlet tube, 10-water outlet tube and 11-blow-off tube.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
As shown in fig. 1, the diversified heat exchange reactor without open flame comprises a cylinder 1 and a support 2, wherein the cylinder 1 is arranged on the support 2, a heat exchange tube 3, a partition plate 4 and a methanol oxidation catalyst 5 are arranged in the cylinder 1, the methanol oxidation catalyst 5 is filled in the cylinder 1, the surface of the methanol oxidation catalyst is coated with rare earth metals, the side wall of one end of the cylinder 1 is provided with an air inlet tube 6, an oil inlet tube 7 and an air outlet tube 8, the front end of the oil inlet tube 7 extends into the air inlet tube 6, the air inlet tube 6 and the air outlet tube 8 are respectively positioned at two sides of the partition plate 4, the bottom end and the top end of the cylinder 1 are respectively provided with an inlet tube 9 and an outlet tube 10 which are communicated with two ends of the.
When the device is used, the methanol is atomized by the atomizer and then is fed into the oil inlet pipe 7, the air is blown into the air inlet pipe 6 by the air blower, the atomized methanol and the methanol oxidation catalyst 5 are triggered to perform oxidation reaction by using the wind speed and the wind pressure, the oxidized methanol and the methanol oxidation catalyst are oxidized into carbon dioxide and water vapor, and simultaneously chemical heat energy is released to heat the water in the heat exchange pipe 3. Meanwhile, the hot air from the air outlet pipe 8 can be used for heating, cold water preheating or hot water heat preservation recycling, so that the energy utilization rate is improved
The utility model discloses utilize alkene organic compound to carry out oxidation reaction and release the chemico-thermal, realize not producing the pollutant to the heating of medium, safety ring protects, energy-conservation is high-efficient, can replace high energy consumption, high pollution, high dangerous coal-fired, fuel, gas, living beings and electric boiler, has extensive suitability.
It will be apparent to those skilled in the art that various changes and modifications may be made without departing from the spirit and scope of the invention. Thus, if such modifications and variations of the present invention fall within the scope of the claims and their equivalents, the present invention is also intended to include such modifications and variations.
Claims (2)
1. There is not pluralism heat exchange reactor of naked light, including barrel, support, the barrel is established on the support, its characterized in that, be equipped with heat exchange tube, baffle and methyl alcohol oxidation catalyst in the barrel, methyl alcohol oxidation catalyst surface cladding has rare earth metal, the one end lateral wall of barrel is equipped with the air-supply line, advances oil pipe, goes out the tuber pipe, the front end that advances oil pipe stretches into in the air-supply line, play tuber pipe are located respectively the both sides of baffle, the bottom of barrel, top be equipped with respectively with inlet tube, the outlet pipe of the both ends intercommunication of heat exchange tube, the bottom of barrel is the blow off pipe in addition.
2. The open-flame-free multiple heat exchange reactor according to claim 1, wherein the methanol oxidation catalyst is filled in the cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022413162.1U CN213631036U (en) | 2020-10-27 | 2020-10-27 | Diversified heat exchange reactor without open fire |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022413162.1U CN213631036U (en) | 2020-10-27 | 2020-10-27 | Diversified heat exchange reactor without open fire |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213631036U true CN213631036U (en) | 2021-07-06 |
Family
ID=76624622
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022413162.1U Active CN213631036U (en) | 2020-10-27 | 2020-10-27 | Diversified heat exchange reactor without open fire |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213631036U (en) |
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2020
- 2020-10-27 CN CN202022413162.1U patent/CN213631036U/en active Active
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