CN105174304B - Ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace - Google Patents
Ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace Download PDFInfo
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- CN105174304B CN105174304B CN201510582914.8A CN201510582914A CN105174304B CN 105174304 B CN105174304 B CN 105174304B CN 201510582914 A CN201510582914 A CN 201510582914A CN 105174304 B CN105174304 B CN 105174304B
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- oxidation furnace
- furnace body
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- energy
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- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 59
- 230000003647 oxidation Effects 0.000 title claims abstract description 58
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 title claims abstract description 18
- 238000004134 energy conservation Methods 0.000 title claims abstract description 13
- 239000002994 raw material Substances 0.000 claims abstract description 13
- 238000010438 heat treatment Methods 0.000 claims abstract description 12
- 230000000694 effects Effects 0.000 claims abstract description 6
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims abstract description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000000835 fiber Substances 0.000 claims abstract description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- 238000009825 accumulation Methods 0.000 claims description 9
- 238000005057 refrigeration Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 6
- 230000008859 change Effects 0.000 claims description 5
- 230000005855 radiation Effects 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 11
- 238000009413 insulation Methods 0.000 abstract description 6
- 230000001590 oxidative effect Effects 0.000 abstract description 3
- 238000007664 blowing Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 abstract description 2
- 230000008569 process Effects 0.000 abstract description 2
- 238000003912 environmental pollution Methods 0.000 abstract 1
- 238000001816 cooling Methods 0.000 description 6
- 230000015556 catabolic process Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 206010054949 Metaplasia Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 206010016766 flatulence Diseases 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000015689 metaplastic ossification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G21/00—Compounds of lead
- C01G21/02—Oxides
- C01G21/10—Red lead (Pb3O4)
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Abstract
The invention discloses a kind of ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace, including an oxidation furnace body, oxidation furnace body 1 is cylindrical structure, and this oxidation furnace body is divided into upper furnace body, middle body of heater and lower volume from top to bottom；Oxidation furnace body exterior uses alumina silicate fiber felt around wrapping, to reaching the effect of insulation and sound insulation, and uses four foot supports to fix.The present invention be by electrical heating produce heat under the blowing of roots blower, be directly sent in oxidation furnace through defeated heat pipe, to raw material heat supply.Can clean production, evade environmental pollution, can realize again quickly preparing Plumbum preparatium, improve production efficiency, by utilization of energy to maximizing, realize oxidizing process by microcomputer control simultaneously, evade occupational hazards, guarantee employee's is healthy.
Description
Technical field
The present invention relates to oxidation furnace technical field, be specifically related to a kind of ground-to-air missile energy-conservation oxidation of formula Plumbum preparatium
Stove.
Background technology
The most advanced Plumbum preparatium oxidation furnace have " vertical read-lead mobile oxidation furnace " (patent No.:
And " a kind of environmental protection drum-type Plumbum preparatium oxygen utilizing solar energy heating auxiliary electrical heater ZL20110109864.9)
Change stove " (patent No.: ZL201310465139.9).The former is by fuel Heating, through three grades of oxygen
Metaplasia output Plumbum preparatium, this kind of oxidation furnace, there is gas emission to pollute environment, tertiary oxidation overlong time, consumption
Take the energy, increase the defects such as production cost；Although the latter can make full use of solar energy, save the energy,
Reducing production cost, raw material can enjoy impartial oxidizing condition (temperature and oxygen) in oxidation furnace,
Shorten oxidization time, improve yield；But this kind of oxidation furnace is during using, due to internal layer stove
Body is overweight, and the most uninterrupted rotation needs certain power, and is easily damaged parts, maintenance cost
Higher, it is important that maintenance idle cost is relatively big, additionally this oxidation furnace either solar energy heating or electricity
Heating is all by the heating to body of heater, then re-supplies to raw material by the heat that body of heater produces, therefore exists
Certain waste is had in utilization of energy.
Summary of the invention
The technical problem to be solved is to provide a kind of scientific structure, rationally, can be used for scale
Change and produce continuously, improve the ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace of production efficiency.
The technical problem to be solved realizes by the following technical solutions:
A kind of ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace, including an oxidation furnace body, described oxidation furnace is originally
Body is cylindrical structure, and this oxidation furnace body is divided into upper furnace body, middle body of heater and lower furnace from top to bottom
Body；
Described upper furnace body accounts for the 1/5 of oxidation furnace body length, and bore lower is slightly thick (can be according to design
The size of bore depending on production capacity), equipped with hopper above described upper furnace body, hopper and upper furnace body
Joint is equipped with limiter of speed；
It is layered in upper furnace body equipped with backgauge roller (heat accumulation pipe), upper and lower two-layer backgauge roller (heat accumulation pipe)
Crisscross setting, between backgauge roller (heat accumulation pipe), lateral separation is 1.5 centimeters, arranges backgauge roller and (stores
Heat pipe) purpose be to make raw material mutually collide when hopper falls, dispersion fall, be unlikely to rush down flood
Falling of formula, it is possible to allow raw material fully equalization be heated and to absorb the oxygen needed for oxidation；
Described backgauge roller uses heat accumulation pipe to make, and heat accumulation pipe is rubescent because being heated, and plays the effect of accumulation of heat,
And by self constantly dispelling the heat, to keep the harmony of in-furnace temperature, allow oxidation material equalization be heated.
Described middle body of heater accounts for the 3.5/5 of oxidation furnace body length, and relative aperture upper furnace body is slightly thin, in
Between the side of body of heater leave at heat inlet three that (quantity of heat inlet can be according to production capacity and the length of body of heater
Fixed), connect in stretching into body of heater by heat inlet is spiral thermal-collecting tube, described thermal-collecting tube side down
To leaving some heat radiation air ports, directly to the raw material heat supply in oxidation furnace body and provide oxidation required oxygen,
Being connected by gate valve outside described heat inlet and have defeated heat pipe, described defeated heat pipe lower inner is equipped with electrical heating core
(market-ripe equipment), electrical heating core is entangled by defeated heat pipe, and air intake is left in side, described defeated heat pipe lower end
Mouthful, this air inlet is respectively led to the heat inlet of oxidation furnace body by roots blower air feed, the upper end of defeated heat pipe；
Direction with about heat inlet 90 degree is respectively kept with air outlet, on the position of air outlet and the position of heat inlet
Lower staggered, (it is positioned at body of heater) inside air outlet equipped with retaining guard, in case material is by air-introduced machine sucking-off,
Connecting induced duct outside air outlet, induced duct leads to air-introduced machine, then leads to cleaner unit；
Described lower volume is the pyramidal structure of mouth down, and length accounts for the 0.5/5 of oxidation furnace body, bottom
Bottom of furnace body is blanking port, connects refrigeration system, refrigeration system carry out raw material below described blanking port
Cooling, is provided with limiter of speed, the limit at this limiter of speed and hopper above between refrigeration system and blanking port
Speed device synchronizes；Finished product after cooling enters storage bin, and connection hexagonal reel below storage bin, hexagonal reel is
By Motor Control, equipped with eccentric on motor, by guide rod connecting eccentric wheel and a hexagonal reel,
Make hexagonal reel ceaselessly move back and forth, make the finished product after cooling fall directly on preset packaging by material blanking tube
In bag or container, the screen cloth of certain hexagonal reel can be exchanged according to customer demand, to meet customer need.
Described defeated heat pipe and the equal subsection setup of induced duct, all connected by corrugated tube between every two sections, with suitable
The change that should expand with heat and contract with cold, protects defeated heat pipe and induced duct.
Mounting temperature sensor at described heat inlet, described gate valve is controlled by temperature detect switch (TDS), set into
Entering the temperature in stove is 450 DEG C-500 DEG C, is automatically switched off gate valve during higher than 500 DEG C, during less than 450 DEG C, and report
Alert device sounds to warn, it is simple to searches reason in time and fixes a breakdown.
Described oxidation furnace body exterior uses alumina silicate fiber felt cincture wrapping, to reaching insulation and sound insulation
Effect, and use four foot supports to fix.
The invention has the beneficial effects as follows: the present invention is heat the blowing at roots blower electrical heating produced
Under, it is directly sent in oxidation furnace through defeated heat pipe, to raw material heat supply.Production can be cleaned, evade ring
Environment pollution, can realize again quickly preparing Plumbum preparatium, improves production efficiency, by utilization of energy to maximizing, with
Shi Shixian oxidizing process, by microcomputer control, has evaded occupational hazards, ensures that employee's is healthy.
Accompanying drawing explanation
Fig. 1 is present configuration schematic diagram.
Detailed description of the invention
For the technological means making the present invention realize, creation characteristic, reach purpose and effect and be readily apparent from
Solve, below in conjunction with being specifically illustrating, the present invention is expanded on further.
See Fig. 1: a kind of ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace, including an oxidation furnace body 1, oxygen
Changing furnace body 1 is cylindrical structure, and this oxidation furnace body 1 is divided into upper furnace body 10, intermediate furnace from top to bottom
Body 20 and lower volume 30；Oxidation furnace body 1 is outside uses alumina silicate fiber felt cincture wrapping, to reaching
Insulation and the effect of sound insulation, and use four foot supports to fix.
Upper furnace body 10 accounts for the 1/5 of oxidation furnace body 1 length, and bore lower is slightly thick (can be according to design
The size of bore depending on production capacity), equipped with hopper 101 above upper furnace body 10, hopper 101 and top
Body of heater 10 joint is equipped with the first limiter of speed 102；In upper furnace body 10, layering is equipped with backgauge roller 103, on
Lower two-layer backgauge roller 103 becomes upper and lower crisscross setting, and between backgauge roller 103, lateral separation is 1.5 centimeters,
The purpose arranging backgauge roller 103 is to make raw material mutually collide when hopper 101 falls, and dispersion is fallen,
It is unlikely to rush down falling of flood formula, it is possible to allow raw material fully equalization be heated and to absorb the oxygen needed for oxidation.
Middle body of heater 20 accounts for the 3.5/5 of oxidation furnace body 1 length, and relative aperture upper furnace body 10 is slightly thin,
The side of middle body of heater 20 leaves at heat inlet 201 3 that (quantity of heat inlet 201 can be according to production capacity and stove
Depending on the length of body), connect in stretching into body of heater by heat inlet 201 is spiral thermal-collecting tube 202, collection
Some heat radiation air ports are left in heat pipe 202 direction down, directly to the raw material heat supply in oxidation furnace body 1
And provide oxidation required oxygen；Connected by gate valve 203 outside heat inlet 201 and have defeated heat pipe 204, defeated heat pipe
204 lower inner are equipped with electrical heating core 205 (market-ripe equipment), and electrical heating core 205 is by defeated heat pipe 204
Entangling, air inlet 206 is left in side, defeated heat pipe 204 lower end, and this air inlet 206 is by roots blower air feed, defeated
The upper end of heat pipe 205 respectively leads to the heat inlet 201 of oxidation furnace body 1；Temperature is installed at heat inlet 201 pass
Sensor (does not indicates in figure), and gate valve 203 is controlled by temperature detect switch (TDS), and the temperature being set in stove is
450 DEG C-500 DEG C, being automatically switched off gate valve during higher than 500 DEG C, during less than 450 DEG C, alarm sounds to warn
Show, it is simple to search reason in time and fix a breakdown.It is respectively kept with at three with the direction of heat inlet about 201 90 degree
Air outlet 207, the position of air outlet 207 interlocks up and down with the position of heat inlet 201, inside air outlet 207
(being positioned at body of heater) is equipped with retaining guard 208, in case material is by air-introduced machine sucking-off, outside air outlet 207
Connecting induced duct 209, induced duct 209 leads to air-introduced machine 210, then leads to cleaner unit 211；Defeated heat pipe 204
Subsection setup equal with induced duct 209, is all connected by corrugated tube 212 between every two sections, cold to adapt to flatulence of heat type
The change of contracting, protects defeated heat pipe 204 and induced duct 209.
The lower volume 30 pyramidal structure in mouth down, length accounts for the 0.5/5 of oxidation furnace body 1, bottom
It is blanking port bottom body of heater 30, connects refrigeration system 40 below blanking port, refrigeration system 40 raw material is entered
Row cooling, is provided with the second limiter of speed 213 between refrigeration system 40 and blanking port, the second limiter of speed 213 and upper
The first limiter of speed 102 at the hopper 101 in face synchronizes；Finished product after cooling enters storage bin, storage bin
Below connection hexagonal reel, hexagonal reel is by Motor Control, equipped with eccentric on motor, logical
Cross guide rod connecting eccentric wheel and a hexagonal reel, make hexagonal reel ceaselessly move back and forth, make the finished product after cooling
Falling directly in preset packaging bag or container by material blanking tube, the screen cloth of certain hexagonal reel can be according to client
Demand is exchanged, to meet customer need.
The ultimate principle of the present invention and principal character and advantages of the present invention have more than been shown and described.One's own profession
Skilled person will appreciate that of industry, the present invention is not restricted to the described embodiments, above-described embodiment and explanation
The principle that the present invention is simply described described in book, without departing from the spirit and scope of the present invention,
The present invention also has various changes and modifications, and these changes and improvements both fall within claimed invention model
In enclosing.Claimed scope is defined by appending claims and equivalent thereof.
Claims (6)
1. a ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace, it is characterised in that include an oxidation furnace body,
This oxidation furnace body is divided into upper furnace body, middle body of heater and lower volume from top to bottom；
Described upper furnace body accounts for the 1/5 of oxidation furnace body length, equipped with hopper above described upper furnace body,
Hopper and upper furnace body joint are equipped with limiter of speed；It is layered equipped with backgauge roller in upper furnace body, every two
Layer backgauge roller becomes upper and lower crisscross setting, and between backgauge roller, lateral separation is 1.5 centimeters；
Described middle body of heater accounts for the 3.5/5 of oxidation furnace body length, leaves into heat in the side of middle body of heater
Mouthful, connecting in stretching into body of heater by heat inlet and have thermal-collecting tube, described thermal-collecting tube direction down is left some
Heat radiation air port, directly to the raw material heat supply in oxidation furnace body and provide oxidation required oxygen, described in enter heat
Being connected by gate valve outside Kou and have defeated heat pipe, described defeated heat pipe lower inner is equipped with electrical heating core, described defeated
Air inlet is left in side, heat pipe lower end, and this air inlet is led to oxygen by roots blower air feed, the upper end of defeated heat pipe
Change the heat inlet of furnace body；Direction with about heat inlet 90 degree is respectively kept with air outlet, the position of air outlet
Put the position with heat inlet to interlock up and down, equipped with retaining guard inside air outlet, connect outside air outlet and draw
Airduct, induced duct leads to air-introduced machine, then leads to cleaner unit；
Described lower volume is the pyramidal structure of mouth down, and length accounts for the 0.5/5 of oxidation furnace body, lower furnace
It is blanking port bottom body, connects refrigeration system below described blanking port, set between refrigeration system and blanking port
Limiter of speed at speed limiter, this limiter of speed and hopper above synchronizes.
Ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace the most according to claim 1, it is characterised in that:
Described thermal-collecting tube is sped structure.
Ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace the most according to claim 1, it is characterised in that:
Described defeated heat pipe and the equal subsection setup of induced duct, all connected by corrugated tube between every two sections.
Ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace the most according to claim 3, it is characterised in that:
Mounting temperature sensor at described heat inlet, described gate valve is controlled by temperature detect switch (TDS), is set into stove
Interior temperature is 450 DEG C-500 DEG C, is automatically switched off gate valve during higher than 500 DEG C, during less than 450 DEG C, and alarm
Sound to warn.
Ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace the most according to claim 1, it is characterised in that:
Described oxidation furnace body exterior uses alumina silicate fiber felt cincture wrapping, and uses four foot supports to fix.
Ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace the most according to claim 1, it is characterised in that:
Described backgauge roller uses heat accumulation pipe to make, and heat accumulation pipe is rubescent because being heated, and plays the effect of accumulation of heat, and leads to
Cross self constantly to dispel the heat, to keep the harmony of in-furnace temperature, allow oxidation material equalization be heated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510582914.8A CN105174304B (en) | 2015-09-14 | 2015-09-14 | Ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510582914.8A CN105174304B (en) | 2015-09-14 | 2015-09-14 | Ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace |
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| Publication Number | Publication Date |
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| CN105174304A CN105174304A (en) | 2015-12-23 |
| CN105174304B true CN105174304B (en) | 2016-10-12 |
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| CN201510582914.8A Active CN105174304B (en) | 2015-09-14 | 2015-09-14 | Ground-to-air missile formula Plumbum preparatium energy-conservation oxidation furnace |
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Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107055593A (en) * | 2017-05-31 | 2017-08-18 | 安徽骏马化工科技股份有限公司 | Ground-to-air missile formula red lead energy-conservation oxidation furnace intelligence thermal controls apparatus |
| CN107098380A (en) * | 2017-05-31 | 2017-08-29 | 安徽骏马化工科技股份有限公司 | Ground-to-air missile formula red lead energy-conservation oxidation furnace intelligence thermal control technique |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2227809Y (en) * | 1995-06-30 | 1996-05-22 | 广州开发区金桥特需化学品与生物工程科技开发公司 | Fluidized-bed oxidation oven for prepn. of chemical-grade manganese oxide |
| CN101780976B (en) * | 2010-01-25 | 2012-01-25 | 张保兴 | Vertical read-lead mobile oxidation furnace |
| CN102297591B (en) * | 2011-07-19 | 2013-05-08 | 青岛福润祥熔炼设备制造有限公司 | High-temperature energy-saving hot air smelting furnace |
| CN205099379U (en) * | 2015-09-14 | 2016-03-23 | 安徽骏马化工科技股份有限公司 | Energy -conserving oxidation furnace of red lead |
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Denomination of invention: Surface-to-air-missile-type red lead energy-saving oxidizing furnace Effective date of registration: 20190104 Granted publication date: 20161012 Pledgee: The development of small and medium-sized enterprises financing Company Limited by Guarantee Jieshou City Pledgor: Anhui Junma New Material Technology Co., Ltd. Registration number: 2018340000803 |
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Date of cancellation: 20200113 Granted publication date: 20161012 Pledgee: The development of small and medium-sized enterprises financing Company Limited by Guarantee Jieshou City Pledgor: Anhui Junma New Material Technology Co., Ltd. Registration number: 2018340000803 |
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Denomination of invention: Surface-to-air-missile-type red lead energy-saving oxidizing furnace Effective date of registration: 20200225 Granted publication date: 20161012 Pledgee: The development of small and medium-sized enterprises financing Company Limited by Guarantee Jieshou City Pledgor: Anhui Junma New Material Technology Co., Ltd. Registration number: Y2020980000335 |
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Denomination of invention: Surface to air missile type red lead energy saving oxidation furnace Effective date of registration: 20210318 Granted publication date: 20161012 Pledgee: The development of small and medium-sized enterprises financing Company Limited by Guarantee Jieshou City Pledgor: Anhui Junma New Material Technology Co.,Ltd. Registration number: Y2021980001782 |