CN209484845U - Methanol oxidation heating equipment - Google Patents
Methanol oxidation heating equipment Download PDFInfo
- Publication number
- CN209484845U CN209484845U CN201920074383.5U CN201920074383U CN209484845U CN 209484845 U CN209484845 U CN 209484845U CN 201920074383 U CN201920074383 U CN 201920074383U CN 209484845 U CN209484845 U CN 209484845U
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- Prior art keywords
- inner tube
- heating
- bucket
- coil
- transferring medium
- Prior art date
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- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title claims abstract description 111
- 238000010438 heat treatment Methods 0.000 title claims abstract description 107
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 27
- 230000003647 oxidation Effects 0.000 title claims abstract description 26
- 239000003054 catalyst Substances 0.000 claims abstract description 16
- 230000008676 import Effects 0.000 claims description 7
- 238000002485 combustion reaction Methods 0.000 description 8
- 239000003921 oil Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 4
- 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
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 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
- 229920000742 Cotton Polymers 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 206010037660 Pyrexia Diseases 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 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
- 239000004744 fabric Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000001788 irregular Effects 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
- 238000004321 preservation Methods 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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- Physical Or Chemical Processes And Apparatus (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model provides a kind of methanol oxidation heating equipment, is related to heating equipment technical field, solves the technical problem that heat exchange area is small, heat exchange efficiency is low.The methanol oxidation heating equipment includes heating bucket, inner tube and two coil pipes, and inner tube setting is in heating bucket；Two coil pipes are located between inner tube and heating bucket along heating bucket axial screw capstan, and two coil pipes are arranged side by side from inside to outside, and two coil pipe one end pass through the first connecting tube respectively and the second connecting tube is connected to inner tube；Catalyst is filled up at the gap of two coil pipes；It further include inlet duct, exhaust apparatus, heat transferring medium gatherer and heat transferring medium guiding device, inlet duct and exhaust apparatus are connected to heating barrel cavity；Heat transferring medium gatherer is connected to inner tube or two coil pipes, and heat transferring medium guiding device is connected to two coil pipe other ends or inner tube.The utility model 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 utility model relates to heating equipment technical fields, more particularly, to a kind of methanol oxidation heating equipment.
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 equipment 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.
Utility model content
The purpose of this utility model is to provide methanol oxidation heating equipments, to solve heat-transfer surface existing in the prior art
The technical problem that product is small, heat exchange efficiency is low.
To achieve the above object, the utility model provides following technical scheme:
A kind of methanol oxidation heating equipment provided by the utility model, including heating bucket, inner tube and coil pipe, the coil pipe
Quantity is two, and respectively the first coil pipe and the second coil pipe, said inner tube are arranged in the heating bucket；Two coil pipes are equal
It is located between said inner tube and the heating bucket along the heating bucket axial screw capstan, and two coil pipes are from inside to outside side by side
Setting, two described coil pipe one end pass through the first connecting tube respectively and the second connecting tube is connected to said inner tube；Two disks
Catalyst is filled up at the gap of pipe；The heating equipment further includes inlet duct, exhaust apparatus, heat transferring medium gatherer and changes
Thermal medium guiding device, the inlet duct and the exhaust apparatus are connected to the heating barrel cavity；The heat transferring medium
Gatherer is connected to said inner tube or two coil pipes, the heat transferring medium guiding device and two coil pipe other ends
Or said inner tube connection.
Said inner tube bottom is provided with mounting under inner tube, said inner tube top as a further improvement of the utility model,
It is provided with mounting in inner tube, the heat transferring medium gatherer is sequentially passed through and sealed in bucket wall and said inner tube on the upside of the heating bucket
Top, middle part, lower part or the bottom of said inner tube inner cavity, first connecting tube and/or second connection are extended to after piece
Pipe protrudes into said inner tube and extends to top, middle part, lower part or the bottom of said inner tube inner cavity.
Said inner tube and the heating bucket is are coaxially disposed as a further improvement of the utility model, and said inner tube
Height is less than the heating bucket height.
Said inner tube both ends pass through three branch in the setting of 120 degree of angles as a further improvement of the utility model,
Frame is connect with the heating bucket, and said inner tube bottom and the heating bucket bottom have interval.
It is provided with mounting at the top of the heating bucket as a further improvement of the utility model, the exhaust apparatus is
Filter screen, the filter screen are arranged on the upper mounting, and the filter screen mesh specification is less than catalyst specification.
The mesh of the filter screen is not more than 6mm as a further improvement of the utility model,.
The heating bucket bottom is provided with lower mounting, the inlet duct packet as a further improvement of the utility model,
Air inlet pipe, methanol dropper and air blower are included, described air inlet pipe one end is threaded through on the lower mounting, the other end and the air blower
Air outlet connection, the methanol dropper is connected in the air inlet pipe.
The import of two coil pipes is located at top or bottom as a further improvement of the utility model, described in two
The outlet of coil pipe is located at bottom or top, first connecting tube and second connecting tube respectively with two coil pipes into
Mouthful connection, the heat transferring medium guiding device be two delivery lines, be arranged in it is described heating barrel side wall lower part or top, two
Described delivery line one end is connect with the outlet of two coil pipes respectively, and two delivery line other ends both pass through the heating
It is extended to after barrel side wall on the outside of the heating bucket.
The heat-conducting medium in the heat transferring medium gatherer is conduction oil as a further improvement of the utility model,.
The heating bucket cross section and said inner tube cross section are circle, just as a further improvement of the utility model,
One of rectangular or rectangle；The shape that two coil pipes surround is identical as said inner tube cross-sectional shape.
The heating bucket is sandwich as a further improvement of the utility model, is vacuum state in sandwich
Or it is filled with heat-preservation cotton.
A kind of heating means heated using the methanol oxidation heating equipment provided by the utility model, including such as
Lower step:
Step A: catalyst is packed into the gap between said inner tube, the heating bucket and two coil pipes；
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 is first into said inner tube or two coil pipes by the heat transferring medium gatherer
Interior progress first time heat exchange, then respectively by the first connecting tube and the second connecting tube enter two coil pipes or it is described in
It carries out exchanging heat for second in pipe, the conduction oil after heating enters heat demand equipment through heat transferring medium guiding device export
In；
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 utility model has the following technical effect that compared with prior art
Inner tube is arranged by the way that two layers of coil pipe is arranged in heating bucket in the utility model among two layers of coil pipe, thermally conductive Jie
Matter is initially entered in inner tube or is once exchanged heat in two coil pipes, and then conduction oil is entered back into two coil pipes or in inner tube
Secondary heat exchange is carried out, by two layers of coil pipe of setting and an inner tube, the heat exchange area inside heating equipment is expanded, increases on the whole
Added the stroke of heat-conducting medium storage level and heat-conducting medium in equipment, under identical equipment volume, heat output it is more efficient,
It is more stable, heat output is bigger；To improve the thermal efficiency of heating equipment；The utility model passes through among two layers of coil pipe
Inner tube is set, so that the catalyst heating conduction at heating bucket center improves, more scientific distributed heat conduction oil deposit is improved
Catalyst service efficiency.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the schematic perspective view of the utility model methanol oxidation heating equipment；
Fig. 2 is the perspective view of the utility model methanol oxidation heating equipment；
Fig. 3 is the sectional view of the utility model methanol oxidation heating equipment.
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；31, the first coil pipe；32, the second coil pipe；4, the first connecting tube；5, filter screen；6, inlet duct；61, air inlet pipe；62, first
Alcohol dropper；63, air blower；7, delivery line；8, ingress pipe；9, the second connecting tube.
Specific embodiment
To keep the purpose of this utility model, technical solution and advantage clearer, below by the technology to the utility model
Scheme is described in detail.Obviously, the described embodiments are only a part of the embodiments of the utility model, rather than all
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are not before making creative work
Obtained all other embodiment is put, the range that the utility model is protected is belonged to.
As shown in Figure 1, the utility model provides a kind of methanol oxidation heating equipment, including heating bucket 1, inner tube 2 and disk
Pipe 3, the quantity of coil pipe 3 are two, and respectively the first coil pipe 31 and the second coil pipe 32, heating bucket 1 are vertical bucket body structure, inner tube
In heating bucket 1,2 axis of inner tube is parallel with heating 1 axis of bucket for 2 settings；First coil pipe 31 and the second coil pipe 32 are along heating bucket 1
Axial screw capstan is located between inner tube 2 and heating bucket 1, and stacking is set side by side from inside to outside for the first coil pipe 31 and the second coil pipe 32
It sets, two 3 one end of coil pipe pass through the first connecting tube 4 respectively and the second connecting tube 9 is connected to inner tube 2；First coil pipe 31 and second
Catalyst is filled up at the gap of coil pipe 32；Heating equipment further includes inlet duct 6, exhaust apparatus, heat transferring medium gatherer
With heat transferring medium guiding device, inlet duct 6 and exhaust apparatus are connected to heating 1 inner cavity of bucket；Heat transferring medium gatherer with
Inner tube 2 or two coil pipes 3 are connected to, and heat transferring medium guiding device is connected to two 3 other ends of coil pipe or inner tube 2.
By being stacked the first coil pipe 31 and the second coil pipe 32 from inside to outside in heating bucket 1, and in innermost layer the
Original fixed column is changed to inner tube 2 by one coil pipe, 31 inside, so that the position at heating 1 center of bucket is also fully utilized, and is passed through
Two layers of coil pipe 3 and inner tube are set, but also the heat of the catalyst release of different location can be exported in heating bucket 1, especially
It is heating 1 central area of bucket, in the prior art due to being that fixed column is unutilized among coil pipe 3, so coil pipe 3 is close to centre
The reaction heat of region often catalyst can not be by timely heat exchange export, so that the heating efficiency of heating equipment is not high, by above
Structure design, heat transferring medium can enter in inner tube 2 with carry out heat exchange on the outside of inner tube 2, to increase changing for heating equipment
Heat area, extends the stroke and reserves of heat transferring medium, to greatly improve heat exchange efficiency and the catalyst utilization of heating equipment
Rate.In the above structure, heat transferring medium by heat transferring medium gatherer import after enter in inner tube 2 or two coil pipes 3 into
The primary heat exchange of row, then enters back into and carries out secondary heat exchange into two coil pipes 3 or inner tube 2, finally by heat transferring medium guiding device
Export.
It should be noted that in the present invention, heat transferring medium gatherer is connected to inner tube 2, heat transferring medium export
Device is connected to two coil pipes 3, so that heat transferring medium is imported into inner tube 2 through heat transferring medium gatherer, is then connected through first
Adapter tube 4 and the second connecting tube 9 enter in the first coil pipe 31 and the second coil pipe 32, most export afterwards through 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, the first connecting tube 4 and/or the second connecting tube 9 protrude into inner tube 2 and extend to inner tube
Top, middle part, lower part or the bottom of 2 inner cavities；In the present invention, the first connecting tube 4 is passed through and is protruded into after mounting 22 in inner tube
Into inner tube 2, the second connecting tube 9 enters in inner tube 2 after passing through side wall of the inner tube.It should be noted that heat transferring medium imports dress
It is set to ingress pipe 8, the depth that ingress pipe 8 is extend into inner tube 2 can select according to actual needs, in the present invention, such as Fig. 3
Shown, ingress pipe 8 extend into 2 bottom of inner tube；The depth that first connecting tube 4 and the second connecting tube 9 are extend into inner tube 2 can also
It selects according to actual needs, in the present invention, the first connecting tube 4 and the second connecting tube 9 extend into the upper of 2 inner cavity of inner tube
Portion.
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
Between top and heating bucket 1 top it is spaced be ingress pipe 8 and the first connecting tube 4 and the second connecting tube 9 for convenience cloth
It sets.
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；It should be noted that in the present invention, the mesh diameter of filter screen 5 is less than 6mm, the mesh of filter screen 5
For circular hole, square hole, delthyrium or irregular shape hole, can specifically select according to the actual situation.Methanol oxidation in heating equipment
The water and carbon dioxide generated after reaction is 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 two coil pipes 3 is located at top or bottom, and the outlet of two coil pipes 3 is located at
Bottom or top, the first connecting tube 4 and the second connecting tube 9 are connect with the import of the first coil pipe 31 and the second coil pipe 32 respectively, are changed
Thermal medium guiding device is the lower part or top that two delivery lines 7 are arranged at heating 1 side wall of bucket, two 7 one end of delivery line point
It is not connect with the outlet of the first coil pipe 31 and the second coil pipe 32, two 7 other ends of delivery line extend to after passing through heating 1 side wall of bucket
Heat 1 outside of bucket.In the present invention, the outlet of two coil pipes 3 is respectively positioned on bottom, and two delivery lines 7 are located at heating 1 side of bucket
Wall bottom.
It should be noted that in the present invention, the heat-conducting medium in heat transferring medium gatherer is conduction oil, certainly
Heat-conducting 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 utility model, as shown in Figure 1, the cross section of heating bucket 1 and inner tube 2 is circle.The shape and inner tube that two coil pipes 3 surround
2 cross-sectional shapes are identical.
The utility model additionally provides a kind of heating means heated using methanol oxidation heating equipment, including as follows
Step:
Step A: catalyst is packed into the gap between inner tube 2, heating bucket 1 and two coil pipes 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 two coil pipes 3 by heat transferring medium gatherer and carries out first
Then secondary heat exchange is entered in two coil pipes 3 or inner tube 2 by the first connecting tube 4 and the second connecting tube 9 and is changed for the second time
Heat, the conduction oil after heating enter in heat demand equipment through the export of heat transferring medium guiding device；
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 utility model is directed to the defect of existing heating equipment, and ladle body internal structure has been greatly improved, has optimized its company
Mode is connect, internal pipeline is increased, increases coil pipe quantity；Therefore under equal volume, heat exchange efficiency and heat utilization efficiency are higher.And
And increase inner tube and coil pipe inside heating staving, the buffering of heat transferring medium can be increased, help to adapt to different working condition；It is interior
The increase of pipe can solve a barrel problem for center catalyst heat conduction efficiency deficiency, and the increase of coil pipe can make in bucket heat exchange area more
It is more, energy conversion rate is improved, and take a firm foundation for heating equipment miniaturization；The utility model is a kind of no flame heating
Equipment mainly makes methanol carry out quick oxidation reaction release heat to heat to conduction oil, is anti-by methanol oxidation
The exothermic reaction answered, 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.
Above description is only a specific implementation of the present invention, but the protection scope of the utility model is not limited to
In this, anyone skilled in the art within the technical scope disclosed by the utility model, can readily occur in variation
Or replacement, it should be covered within the scope of the utility model.Therefore, the protection scope of the utility model should be with the power
Subject to the protection scope that benefit requires.
Claims (10)
1. a kind of methanol oxidation heating equipment, it is characterised in that: including heating bucket (1), inner tube (2) and coil pipe (3), the coil pipe
(3) it is respectively the first coil pipe (31) and the second coil pipe (32) that quantity, which is two, and said inner tube (2) is arranged in the heating bucket
(1) in；Two coil pipes (3) are located at said inner tube (2) and the heating bucket along heating bucket (1) the axial screw capstan
(1) between, and two coil pipes (3) are arranged side by side from inside to outside, and two described coil pipe (3) one end pass through the first connection respectively
Pipe (4) and the second connecting tube (9) are connected to said inner tube (2)；Catalyst is filled up at the gap of two coil pipes (3)；It is described
Heating equipment further includes inlet duct (6), exhaust apparatus, heat transferring medium gatherer and heat transferring medium guiding device, it is described into
Device of air (6) and the exhaust apparatus are connected to heating bucket (1) inner cavity；The heat transferring medium gatherer with it is described interior
Manage (2) or two coil pipes (3) connections, the heat transferring medium guiding device and two coil pipe (3) other ends or described
Inner tube (2) connection.
2. methanol oxidation heating equipment 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, first connecting tube (4) and/or second connecting tube (9) protrude into said inner tube (2) and extend to institute
State top, middle part, lower part or the bottom of inner tube (2) inner cavity.
3. methanol oxidation heating equipment 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 equipment 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 equipment 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 equipment according to claim 5, it is characterised in that: the mesh of the filter screen (5) is little
In 6mm.
7. methanol oxidation heating equipment according to claim 1, it is characterised in that: the import position of two coil pipes (3)
In top or bottom, the outlet of two coil pipes (3) is located at bottom or top, first connecting tube (4) and described second
Connecting tube (9) is connect with the import of two coil pipes (3) respectively, and the heat transferring medium guiding device is two delivery lines (7),
Be arranged it is described heating bucket (1) side wall lower part or top, two described delivery line (7) one end respectively with two coil pipes
(3) outlet connection, two delivery line (7) other ends extend to the heating after both passing through heating bucket (1) side wall
On the outside of bucket (1).
8. methanol oxidation heating equipment 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 that two coil pipes (3) surround with it is described
Inner tube (2) cross-sectional shape is identical.
9. methanol oxidation heating equipment 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).
10. methanol oxidation heating equipment according to claim 1, it is characterised in that: in the heat transferring medium gatherer
Heat-conducting medium be conduction oil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920074383.5U CN209484845U (en) | 2019-01-16 | 2019-01-16 | Methanol oxidation heating equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920074383.5U CN209484845U (en) | 2019-01-16 | 2019-01-16 | Methanol oxidation heating equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209484845U true CN209484845U (en) | 2019-10-11 |
Family
ID=68131337
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920074383.5U Active CN209484845U (en) | 2019-01-16 | 2019-01-16 | Methanol oxidation heating equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209484845U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109539555A (en) * | 2019-01-16 | 2019-03-29 | 佛山市无火发热新能源科技有限公司 | Methanol oxidation heating equipment and heating means |
| CN114893911A (en) * | 2022-06-01 | 2022-08-12 | 镇江威斯康电器有限公司 | Explosion-proof forced air electric heater |
-
2019
- 2019-01-16 CN CN201920074383.5U patent/CN209484845U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109539555A (en) * | 2019-01-16 | 2019-03-29 | 佛山市无火发热新能源科技有限公司 | Methanol oxidation heating equipment and heating means |
| CN114893911A (en) * | 2022-06-01 | 2022-08-12 | 镇江威斯康电器有限公司 | Explosion-proof forced air electric heater |
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