CN109539556A - Methanol oxidation heating device and heating means - Google Patents
Methanol oxidation heating device and heating means Download PDFInfo
- Publication number
- CN109539556A CN109539556A CN201910042325.9A CN201910042325A CN109539556A CN 109539556 A CN109539556 A CN 109539556A CN 201910042325 A CN201910042325 A CN 201910042325A CN 109539556 A CN109539556 A CN 109539556A
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- Prior art keywords
- inner tube
- heating
- coil pipe
- bucket
- heating bucket
- 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.)
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- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title claims abstract description 117
- 238000010438 heat treatment Methods 0.000 title claims abstract description 111
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 26
- 230000003647 oxidation Effects 0.000 title claims abstract description 24
- 239000003054 catalyst Substances 0.000 claims abstract description 17
- 230000008676 import Effects 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 4
- 238000006555 catalytic reaction Methods 0.000 claims description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 2
- 239000001569 carbon dioxide Substances 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- 239000008246 gaseous mixture Substances 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 description 8
- 239000003921 oil Substances 0.000 description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- TVEXGJYMHHTVKP-UHFFFAOYSA-N 6-oxabicyclo[3.2.1]oct-3-en-7-one Chemical compound C1C2C(=O)OC1C=CC2 TVEXGJYMHHTVKP-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 206010037660 Pyrexia Diseases 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H7/00—Storage heaters, i.e. heaters in which the energy is stored as heat in masses for subsequent release
- F24H7/02—Storage heaters, i.e. heaters in which the energy is stored as heat in masses for subsequent release the released heat being conveyed to a transfer fluid
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/18—Arrangement or mounting of grates or heating means
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The present invention provides a kind of methanol oxidation heating device and heating means, are related to heating equipment technical field, solve the technical problem that heat exchange area is small, heat exchange efficiency is low.The methanol oxidation heating device includes heating bucket, inner tube and coil pipe, and inner tube setting is in heating bucket；Coil pipe is located between inner tube and heating bucket along heating bucket axial screw capstan, and coil pipe one end is connected to by connecting tube with inner tube；Catalyst is filled up at the gap of coil pipe；Heating device further includes inlet duct, exhaust apparatus, heat transferring medium gatherer and heat transferring medium guiding device, and inlet duct and exhaust apparatus are connected to heating barrel cavity；Heat transferring medium gatherer is connected to inner tube or coil pipe, and heat transferring medium guiding device is connected to the coil pipe other end or inner tube.The present invention expands the stroke of heat exchange area, heat-conducting medium storage level and heat-conducting medium in equipment, improves heat exchange efficiency.
Description
Technical field
The present invention relates to heating equipment technical fields, more particularly, to a kind of methanol oxidation heating device and heating means.
Background technique
China obtains heat using boiler on a large scale in manufacturing each fields such as industry, service trade, people's livelihood life at present
Energy.Boiler is a kind of to obtain the device of heat in the way of heating by the temperature of flame by burning fuel.The combustion
Material includes natural gas, coal, fuel oil, firewood, biological particles, methanol.It is heated using these fuel combustions, existing defect is such as
Under: combustion reaction is insufficient, imperfect combustion occurs；Furthermore harmful substance can be discharged, such as: sulfur oxide, nitrogen oxide, an oxidation
Carbon, fine particulates etc. have seriously affected air quality, welding；Although combustion of natural gas is relatively clean, its pipe network
Majority concentrates on down town, it is difficult to cover full scope.
In order to solve a series of problems present in combustion heating, currently on the market, there is a kind of flameless combustion device,
The new heating method of thermal energy can be obtained without burning fuel, this flameless combustion device is carried out in reactor using methanol
The device that catalysis reaction is heated.
Applicants have discovered that at least there is following technical problem in the prior art:
Methanol oxidation heating device in the prior art has the following technical problems that heating bucket internal heat transfer surface area is small, changes
The thermal efficiency is not high；Catalyst utilization is low.
Summary of the invention
The purpose of the present invention is to provide methanol oxidation heating device and heating means, existing in the prior art to solve
The technical problem that heat exchange area is small, heat exchange efficiency is low.
To achieve the above object, the present invention provides following technical schemes:
A kind of methanol oxidation heating device provided by the invention, including heating bucket, inner tube and coil pipe, said inner tube setting exist
In the heating bucket；The coil pipe is located between said inner tube and the heating bucket along the heating bucket axial screw capstan, and institute
Coil pipe one end is stated to be connected to by connecting tube with said inner tube；Catalyst is filled up at the gap of the coil pipe；The heating device is also
Including inlet duct, exhaust apparatus, heat transferring medium gatherer and heat transferring medium guiding device, the inlet duct and the row
Device of air is connected to the heating barrel cavity；The heat transferring medium gatherer is connected to said inner tube or the coil pipe, institute
Heat transferring medium guiding device is stated to be connected to the coil pipe other end or said inner tube.
As a further improvement of the present invention, said inner tube bottom is provided with mounting under inner tube, setting at the top of said inner tube
There is mounting in inner tube, the heat transferring medium gatherer sequentially passes through in the heating bucket upside bucket wall and said inner tube after mounting
Top, middle part, lower part or the bottom of said inner tube inner cavity are extended to, the connecting tube is passed through and extended to after mounting in said inner tube
Top, middle part, lower part or the bottom of said inner tube inner cavity.
As a further improvement of the present invention, said inner tube and the heating bucket is are coaxially disposed, and said inner tube height
Less than the heating bucket height.
As a further improvement of the present invention, said inner tube both ends pass through three in 120 degree angles setting bracket and
The heating bucket connection, and said inner tube bottom and the heating bucket bottom have interval.
As a further improvement of the present invention, mounting is provided at the top of the heating bucket, the exhaust apparatus is filtering
Net, the filter screen are arranged on the upper mounting, and the filter screen mesh specification is less than catalyst specification.
As a further improvement of the present invention, the heating bucket bottom is provided with lower mounting, the inlet duct include into
Tracheae, methanol dropper and air blower, described air inlet pipe one end are threaded through on the lower mounting, and the other end goes out with the air blower
Air port connection, the methanol dropper are connected in the air inlet pipe.
As a further improvement of the present invention, the import of the coil pipe is located at top or bottom, the outlet position of the coil pipe
In bottom or top, the connecting tube is connect with the import of the coil pipe, and the heat transferring medium guiding device is delivery line setting
In the lower part or top of the heating barrel side wall, described delivery line one end is connect with the outlet of the coil pipe, and the delivery line is another
One end extends on the outside of the heating bucket after passing through the heating barrel side wall.
As a further improvement of the present invention, the heat-conducting medium in the heat transferring medium gatherer is conduction oil.
As a further improvement of the present invention, the heating bucket cross section and said inner tube cross section are round, square
Or one of rectangle；The shape that the coil pipe surrounds is identical as said inner tube cross-sectional shape.
As a further improvement of the present invention, the mesh diameter of the filter screen is not more than 6mm.
A kind of heating means heated using the methanol oxidation heating device provided by the invention, including walk as follows
It is rapid:
Step A: catalyst is packed into the gap between said inner tube, the heating bucket and the coil pipe；
Step B: it enters in the heating bucket after air and methanol mixing through the inlet duct and is urged with catalyst
Change reaction, and discharges heat；
Step C: conduction oil by the heat transferring medium gatherer be first into said inner tube or the coil pipe into
Row exchanges heat for the first time, is then entered in the coil pipe or said inner tube and is exchanged heat by connecting tube for second of progress, after heating
Conduction oil enters in heat demand equipment through heat transferring medium guiding device export；
Step D: the catalysis of the gaseous mixture and catalyst of methanol and air generates water and carbon dioxide through institute after the reaction was completed
Exhaust apparatus is stated to be discharged to outside the heating bucket
The present invention has the following technical effect that compared with prior art
The present invention is initially entered in inner tube and is carried out once by the way that inner tube, heat-conducting medium are arranged among the coil pipe in heating bucket
Heat exchange, then conduction oil, which enters back into, carries out secondary heat exchange in coil pipe, by the way that inner tube is arranged, expands changing inside heating device
Heat area increases the stroke of heat-conducting medium storage level and heat-conducting medium in equipment on the whole, under identical equipment volume, heat
Amount output is more efficient, more stable, heat output is bigger；To improve the thermal efficiency of heating device；The present invention by
Inner tube is set among coil pipe, and more scientific distributed heat conduction oil deposit improves catalyst service efficiency.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
Some embodiments of invention for those of ordinary skill in the art without creative efforts, can be with
It obtains other drawings based on these drawings.
Fig. 1 is the schematic perspective view of methanol oxidation heating device of the present invention；
Fig. 2 is that methanol oxidation heating device of the present invention is dismantled the top view after filter screen；
Fig. 3 is AA cross-sectional view in Fig. 2.
1 in figure, heat bucket；11, upper mounting；2, inner tube；21, mounting under inner tube；22, mounting in inner tube；23, bracket；3,
Coil pipe；4, connecting tube；5, filter screen；6, inlet duct；61, air inlet pipe；62, methanol dropper；63, air blower；7, delivery line；8,
Ingress pipe.
Specific embodiment
To make the object, technical solutions and advantages of the present invention clearer, technical solution of the present invention will be carried out below
Detailed description.Obviously, described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.Base
Embodiment in the present invention, those of ordinary skill in the art are obtained all without making creative work
Other embodiment belongs to the range that the present invention is protected.
As shown in Figure 1, the present invention provides a kind of methanol oxidation heating device, including heating bucket 1, inner tube 2 and coil pipe 3,
Heating bucket 1 is vertical bucket body structure, and for the setting of inner tube 2 in heating bucket 1,2 axis of inner tube is parallel with heating 1 axis of bucket；3 edge of coil pipe
Heating 1 axial screw capstan of bucket is located between inner tube 2 and heating bucket 1, and 3 one end of coil pipe is connected to by connecting tube 4 with inner tube 2；Disk
Catalyst is filled up at the gap of pipe 3；Heating device further includes inlet duct 6, exhaust apparatus, heat transferring medium gatherer and heat exchange
Medium guiding device, inlet duct 6 and exhaust apparatus are connected to heating 1 inner cavity of bucket；Heat transferring medium gatherer and inner tube 2 or
Coil pipe 3 is connected to, and heat transferring medium guiding device is connected to 3 other end of coil pipe or inner tube 2.
By the way that inner tube 2 is arranged in 3 intermediate region of coil pipe so that 3 intermediate region of coil pipe is also utilized, and heat transferring medium into
Enter into inner tube 2 the reaction heat progress heat exchange with 2 outside of inner tube to extend to increase the heat exchange area of heating device
The stroke and reserves of heat transferring medium, to greatly improve the heat exchange efficiency and catalyst utilization of heating device.In the above structure
In, heat transferring medium is entered in inner tube 2 or coil pipe 3 after being imported by heat transferring medium gatherer and is once exchanged heat, then again
It enters in coil pipe 3 or inner tube 2 and carries out secondary heat exchange, finally exported by heat transferring medium guiding device.
As an alternative embodiment, 2 bottom of inner tube is provided with mounting 21 under inner tube, it is provided at the top of inner tube 2 interior
Mounting 22 on pipe, heat transferring medium gatherer sequentially pass through and extend to inner tube 2 after mounting 22 in heating 1 upside bucket wall of bucket and inner tube
Top, middle part, lower part or the bottom of inner cavity, connecting tube 4 pass through extended to after mounting 22 in inner tube 2 inner cavity of inner tube top, in
Portion, lower part or bottom.It should be noted that heat transferring medium gatherer is ingress pipe 8, ingress pipe 8 extend into the depth in inner tube 2
Degree can select according to actual needs, in the present invention, as shown in figure 3, ingress pipe 8 extend into 2 bottom of inner tube；Connecting tube 4 protrudes into
It can also be selected according to actual needs to the depth in inner tube 2, in the present invention, connecting tube 4 extend into the top of 2 inner cavity of inner tube.
As shown in figure 3, inner tube 2 and heating bucket 1 are coaxial arrangement, and 2 height of inner tube is less than 1 height of heating bucket.Inner tube 2 is pushed up
Between portion and heating bucket 1 top it is spaced be ingress pipe 8 and connecting tube 4 for convenience arrangement.
It is connect as shown in Fig. 2, 2 both ends of inner tube pass through three brackets 23 in the setting of 120 degree of angles with heating bucket 1, and
2 bottom of inner tube and heating 23 bottom of bucket have interval.The interval is for placing the atomizer in inlet duct 6, air inlet pipe 61
It is connected to atomizer.
It is provided with mounting 11 at the top of heating bucket 1, opening is provided on upper mounting 11, exhaust apparatus is filter screen 5, filtering
The opening on upper mounting 11 is arranged in net 5, and catalyst drops out from filter screen 5 in order to prevent, and 5 mesh specification of filter screen is less than
Catalyst specification；In the present invention, the mesh diameter of filter screen 5 is not more than 6mm.It is raw after methanol oxidation reaction in heating device
At water and carbon dioxide be discharged in atmosphere from filter screen 5 through chimney.
As optional embodiment, heats 1 bottom of bucket and be provided with lower mounting, inlet duct 6 includes air inlet pipe 61, methanol
Dropper 62 and air blower 63,61 one end of air inlet pipe are threaded through on lower mounting, and the other end is connect with the air outlet of air blower 63, methanol
Dropper 62 is connected in air inlet pipe 61.6 in inlet duct, it is in liquid pearl in 61 wall of air inlet pipe that methanol, which instills, is located at air inlet pipe
The wind impact that the air blower 63 of 61 other ends is blown out nebulizes and methanol mixed gas, and it is above-mentioned to be then blown into progress in heating bucket 1
Oxidation reaction fever.
As optional embodiment, the import of coil pipe 3 is located at top or bottom, and the outlet of coil pipe 3 is located at bottom or top
Portion, connecting tube 4 are connect with the import of coil pipe 3, and heat transferring medium guiding device is the lower part that heating 1 side wall of bucket is arranged in delivery line 7
Or top, 7 one end of delivery line are connect with the outlet of coil pipe 3,7 other end of delivery line extends to heating after passing through heating 1 side wall of bucket
1 outside of bucket.In the present invention, the outlet of coil pipe 3 is located at bottom, and delivery line 7 is located at heating 1 sidewall bottom of bucket.
It should be noted that in the present invention, the heat-conducting medium in heat transferring medium gatherer is conduction oil, certainly thermally conductive
Medium can also be made of other materials in the prior art.
Further, it heats 1 cross section of bucket and 2 cross section of inner tube is one of round, square or rectangular；At this
In invention, as shown in Figure 1, the cross section of heating bucket 1 and inner tube 2 is circle.The shape and 2 cross section of inner tube that coil pipe 3 surrounds
Shape is identical.
The present invention also provides a kind of heating means heated using methanol oxidation heating device, including walk as follows
It is rapid:
Step A: catalyst is packed into the gap between inner tube 2, heating bucket 1 and coil pipe 3；
Step B: entering to occur to be catalyzed with catalyst in heating bucket 1 and react after air and methanol mixing through inlet duct 6,
And discharge heat；
Step C: conduction oil is first into inner tube 2 or coil pipe 3 by heat transferring medium gatherer change for the first time
Then heat is entered in coil pipe 3 or inner tube 2 by connecting tube 4 and carries out second of heat exchange, the conduction oil after heating is through heat transferring medium
Guiding device export enters in heat demand equipment；
Step D: the catalysis of the gaseous mixture and catalyst of methanol and air generates water and carbon dioxide through arranging after the reaction was completed
Device of air is discharged to outside heating bucket 1.
The present invention is directed to the defect of existing heating device, and ladle body internal structure has been greatly improved, has optimized its connection side
Formula increases internal pipeline；It compares existing, improves 70% heat exchange area of heating bucket, and be former heating bucket heat exchange area
1.7 times；Therefore under equal volume, heat exchange efficiency and heat utilization efficiency are higher.And increase inner tube, Ke Yizeng inside heating staving
The buffering for adding heat transferring medium helps to adapt to different working condition；The increase of inner tube can solve barrel thermally conductive effect of center catalyst
The insufficient problem of energy also improves energy conversion rate, and takes a firm foundation for heating device miniaturization；The present invention is a kind of nothing
Flame heating device mainly makes methanol carry out quick oxidation reaction release heat to heat to conduction oil, is to pass through first
The exothermic reaction of alcohol oxidation reaction, to heat-conducting oil heating, so in its exhaust gas for generating, without harmful substance (sulfur oxide,
Nitrogen oxide, carbon monoxide, finely ground particles etc.), it is a kind of highly-safe, high reliablity, environment amenable innovative device.
The above description is merely a specific embodiment, but scope of protection of the present invention is not limited thereto, any
Those familiar with the art in the technical scope disclosed by the present invention, can easily think of the change or the replacement, and should all contain
Lid is within protection scope of the present invention.Therefore, protection scope of the present invention should be based on the protection scope of the described claims.
Claims (10)
1. a kind of methanol oxidation heating device, it is characterised in that: including heating bucket (1), inner tube (2) and coil pipe (3), said inner tube
(2) setting is in the heating bucket (1)；The coil pipe (3) is located at said inner tube (2) along heating bucket (1) the axial screw capstan
Between the heating bucket (1), and the coil pipe (3) one end is connected to by connecting tube (4) with said inner tube (2)；The coil pipe
(3) catalyst is filled up at gap；The heating device further includes inlet duct (6), exhaust apparatus, heat transferring medium gatherer
With heat transferring medium guiding device, the inlet duct (6) and the exhaust apparatus are connected to heating bucket (1) inner cavity；Institute
It states heat transferring medium gatherer to be connected to said inner tube (2) or the coil pipe (3), the heat transferring medium guiding device and the disk
Manage (3) other end or said inner tube (2) connection.
2. methanol oxidation heating device according to claim 1, it is characterised in that: in said inner tube (2) bottom is provided with
It manages lower mounting (21), is provided with mounting in inner tube (22) at the top of said inner tube (2), the heat transferring medium gatherer sequentially passes through
Extended to after mounting (22) in bucket wall and said inner tube on the upside of heating bucket (1) top of said inner tube (2) inner cavity, middle part,
Lower part or bottom, the connecting tube (4) pass through extended to after mounting (22) in said inner tube said inner tube (2) inner cavity top,
Middle part, lower part or bottom.
3. methanol oxidation heating device according to claim 1, it is characterised in that: said inner tube (2) and the heating bucket
It (1) is coaxial arrangement, and said inner tube (2) is highly less than heating bucket (1) height.
4. methanol oxidation heating device according to claim 1 or 2 or 3, it is characterised in that: said inner tube (2) both ends are equal
By three in 120 degree angles be arranged bracket (23) connect with the heating bucket (1), and said inner tube (2) bottom with it is described
Heating bucket (1) bottom has interval.
5. methanol oxidation heating device according to claim 1, it is characterised in that: be provided at the top of the heating bucket (1)
Upper mounting (11), the exhaust apparatus are filter screen (5), and the filter screen (5) is arranged on the upper mounting (11), the mistake
Strainer (5) mesh specification is less than catalyst specification.
6. methanol oxidation heating device according to claim 1, it is characterised in that: heating bucket (1) bottom is provided with
Lower mounting (12), the inlet duct (6) include air inlet pipe (61), methanol dropper (62) and air blower (63), the air inlet pipe
(61) one end is threaded through on the lower mounting (12), and the other end is connect with the air outlet of the air blower (63), the methanol drop
Pipe (62) is connected on the air inlet pipe (61).
7. methanol oxidation heating device according to claim 1, it is characterised in that: the import of the coil pipe (3) is located at top
Portion or bottom, the outlet of the coil pipe (3) are located at bottom or top, and the import of the connecting tube (4) and the coil pipe (3) connects
Connect, the heat transferring medium guiding device be delivery line (7) be arranged it is described heating bucket (1) side wall lower part or top, it is described to lead
Outlet pipe (7) one end is connect with the outlet of the coil pipe (3), after delivery line (7) other end passes through heating bucket (1) side wall
It extends on the outside of the heating bucket (1).
8. methanol oxidation heating device according to claim 1, it is characterised in that: the heating bucket (1) cross section and institute
Inner tube (2) cross section is stated as one of round, square or rectangular；The shape and said inner tube that the coil pipe (3) surrounds
(2) cross-sectional shape is identical.
9. methanol oxidation heating device according to claim 5, it is characterised in that: the mesh diameter of the filter screen (5)
No more than 6mm.
10. a kind of heating means that the methanol oxidation heating device using as described in any in claim 1-9 is heated,
It is characterized in that: including the following steps:
Step A: will be in the gap between catalyst loading said inner tube (2), heating bucket (1) and the coil pipe (3)；
Step B: it enters in the heating bucket (1) after air and methanol mixing through the inlet duct (6) and occurs with catalyst
Catalysis reaction, and discharge heat；
Step C: conduction oil is first into said inner tube (2) or the coil pipe (3) by the heat transferring medium gatherer
First time heat exchange is carried out, is then entered in the coil pipe (3) or said inner tube (2) by connecting tube (4) and is changed for the second time
Heat, the conduction oil after heating enter in heat demand equipment through heat transferring medium guiding device export；
Step D: the catalysis of the gaseous mixture and catalyst of methanol and air generates water and carbon dioxide through the row after the reaction was completed
Device of air is discharged to the heating bucket (1) outside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910042325.9A CN109539556A (en) | 2019-01-16 | 2019-01-16 | Methanol oxidation heating device and heating means |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910042325.9A CN109539556A (en) | 2019-01-16 | 2019-01-16 | Methanol oxidation heating device and heating means |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109539556A true CN109539556A (en) | 2019-03-29 |
Family
ID=65837840
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910042325.9A Pending CN109539556A (en) | 2019-01-16 | 2019-01-16 | Methanol oxidation heating device and heating means |
Country Status (1)
| Country | Link |
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| CN (1) | CN109539556A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110108032A (en) * | 2019-05-13 | 2019-08-09 | 佛山光腾新能源股份有限公司 | A kind of Teat pump boiler and its working method based on methanol auxiliary heating |
| CN110425906A (en) * | 2019-08-21 | 2019-11-08 | 佛山光腾新能源股份有限公司 | A kind of hot water heating device based on methanol oxidation heating |
| CN110425586A (en) * | 2019-08-21 | 2019-11-08 | 佛山光腾新能源股份有限公司 | A kind of commercial stove based on the catalysis heating of methanol catalyst |
| CN112393450A (en) * | 2020-11-18 | 2021-02-23 | 常州大学 | Methanol outdoor food heating and graphene heating device |
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| CN110108032A (en) * | 2019-05-13 | 2019-08-09 | 佛山光腾新能源股份有限公司 | A kind of Teat pump boiler and its working method based on methanol auxiliary heating |
| CN110425906A (en) * | 2019-08-21 | 2019-11-08 | 佛山光腾新能源股份有限公司 | A kind of hot water heating device based on methanol oxidation heating |
| CN110425586A (en) * | 2019-08-21 | 2019-11-08 | 佛山光腾新能源股份有限公司 | A kind of commercial stove based on the catalysis heating of methanol catalyst |
| CN112393450A (en) * | 2020-11-18 | 2021-02-23 | 常州大学 | Methanol outdoor food heating and graphene heating device |
| CN112393450B (en) * | 2020-11-18 | 2022-03-01 | 常州大学 | Methanol outdoor food heating and graphene heating device |
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