CN206577742U - One kind energy-conservation oxidation unit - Google Patents
One kind energy-conservation oxidation unit Download PDFInfo
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- CN206577742U CN206577742U CN201621275188.1U CN201621275188U CN206577742U CN 206577742 U CN206577742 U CN 206577742U CN 201621275188 U CN201621275188 U CN 201621275188U CN 206577742 U CN206577742 U CN 206577742U
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Abstract
One kind energy-conservation oxidation unit, including oxidation furnace body, the oxidation furnace body is divided into upper furnace body from top to bottom, middle body of heater and lower furnace body, hopper is housed above the upper furnace body, heat inlet is left in the side of middle body of heater, it is symmetrical in oxidation furnace inner body wall to be provided with two baffle plates being obliquely installed, baffle plate is located at below heat inlet, the baffle plate of heat inlet opening direction nearby, defeated heat pipe is connected with outside the heat inlet, leave air inlet in the lower end side of the defeated heat pipe, air inlet side connects oxygen tank, air outlet is respectively kept with 90 degree of direction of heat inlet or so, connection induced duct outside air outlet, induced duct leads to air-introduced machine, lower furnace body bottom is discharging opening, connection refrigeration system below the discharging opening.The utility model be the heat for producing electrical heating under the blowing of blower fan, the oxygen of air and oxygen tank is together sent in oxidation furnace, to raw material heat supply and oxygen supply, can clean manufacturing, can accelerate reaction rate again, improve production efficiency.
Description
Technical field
The utility model is related to oxidation furnaces technical field, and oxidation unit is saved more particularly, to one kind.
Background technology
Slightly advanced red lead oxidation furnace has " vertical read-lead mobile oxidation furnace " (patent No. in the market：
) and a kind of " environment-friendlyrotary rotary drum type red lead oxidizing furnace of utilization solar energy heating auxiliary electrical heater " (patent ZL20110109864.9
Number：ZL201310465139.9).The former is, by fuel Heating, red lead to be produced by tertiary oxidation, and this kind of oxidation furnace has
Gas emission pollutes environment, and tertiary oxidation overlong time expends the energy, increases the defects such as production cost；Although the latter can fill
Divide and utilize solar energy, saved the energy, reduced production cost, raw material can enjoy impartial oxidizing condition in oxidation furnace
(temperature and oxygen), shortens oxidization time, improves yield；But this kind of oxidation furnace is during utilization, due to internal layer stove
Body is overweight, and continuous uninterrupted rotation needs certain power, and is easily damaged parts, and maintenance cost is higher, it is important that
Repair idle cost it is larger, in addition the oxidation furnace either solar energy heating or electrical heating be all by the heating to body of heater,
Then the heat that body of heater is produced is re-supplied to raw material, therefore has in using energy source certain waste.
The A of CN 105174304 disclose a kind of ground-to-air missile formula red lead energy-conservation oxidation furnace, and the oxidation furnace produces electrical heating
Raw heat is directly sent in oxidation furnace under the blowing of roots blower by defeated heat pipe, to raw material heat supply and oxygen supply, although
Energy clean manufacturing, evades environmental pollution, but oxygen content of the oxygen sources needed for reaction in air, air is about
21%, therefore oxidizing reaction rate is low, and can further influence production efficiency.
Utility model content
The technical problems to be solved in the utility model is：Overcoming the deficiencies in the prior art, there is provided a kind of scientific structure, conjunction
Reason, can be used for scale and continuously produce, and accelerate reaction rate, improve the energy-conservation oxidation unit of production efficiency.
The utility model solves the technical scheme that its technical problem used：One kind energy-conservation oxidation unit, including oxidation
Furnace body, the oxidation furnace body is divided into above upper furnace body, middle body of heater and lower furnace body, the upper furnace body from top to bottom is equipped with blanking
Bucket, layering is equipped with backgauge roller in upper furnace body, and heat inlet is left in the side of middle body of heater, is stretched into body of heater and connected by heat inlet
There is a thermal-collecting tube, the thermal-collecting tube direction directed downwardly, which is left, symmetrical in some radiating air ports, oxidation furnace inner body wall is provided with two
The individual baffle plate being obliquely installed, baffle plate is located at below heat inlet, and heat inlet opening connects towards baffle plate nearby, the heat inlet outside
Defeated heat pipe is connected to, air inlet is left in the lower end side of the defeated heat pipe, air inlet side connection oxygen tank, with heat inlet or so 90
The direction of degree, which is respectively kept with the inside of air outlet, air outlet, is equipped with retaining guard, and connection induced duct outside air outlet, induced duct leads to
Air-introduced machine, then leads to deduster, and lower furnace body bottom is connection refrigeration system below discharging opening, the discharging opening.
The hopper and upper furnace body joint are equipped with the first limiter of speed, provided with the between the refrigeration system and discharging opening
Two limiter of speeds, the first limiter of speed and the second limiter of speed are synchronous.
The equal subsection setup of the defeated heat pipe and induced duct, is connected by bellows between every two sections, cold to adapt to heat expansion
The change of contracting, protects defeated heat pipe and induced duct.
The oxidation furnace body exterior surround wrapping using heat preserving and insulating material, to reach the effect of insulation and sound insulation,
And fixed using four foot supports.
Defeated heat pipe, the lock are connected with by gate valve outside mounting temperature sensor at the heat inlet, the heat inlet
Valve is controlled by temperature detect switch (TDS), and the temperature being set into stove is 450 DEG C ~ 500 DEG C, automatic closing gate valve during higher than 500 DEG C,
During less than 450 DEG C, alarm sounds to warn.
The thermal-collecting tube is sped structure.
The defeated heat pipe lower inner is equipped with electrical heating core, and what the upper end of defeated heat pipe respectively led to aoxidize furnace body enters heat
Mouthful.
The position of the air outlet and the position of heat inlet interlock up and down, are conducive to airflow circulating to flow, accelerated oxidation is anti-
Should.
The backgauge roller is made of heat accumulation pipe, and every two layers of backgauge roller is set into crisscross up and down, horizontal between backgauge roller
It is 1.5cm to distance, heat accumulation pipe plays a part of accumulation of heat because heated and rubescent, and is constantly radiated by itself, with holding furnace
The harmony of interior temperature, makes oxidation material equalization heated；The purpose for setting backgauge roller is raw material is fallen phase from hopper
It is mutual to collide, disperse to fall, be unlikely to rush down falling for big vast formula, raw material fully equalization can be allowed to be heated and absorb needed for oxidation
Oxygen.
The oxidation furnace body is cylindrical structure, and the lower furnace body is in the pyramidal structure of mouth down, and the upper furnace body is accounted for
The 1/5 of oxidation furnace body length, the middle body of heater accounts for the 7/10 of oxidation furnace body length, and the lower furnace body length accounts for oxidation furnace
The 1/10 of body.
Depending on the quantity of the middle body of heater side heat inlet can be according to production capacity and the length of body of heater, the number of the air outlet
Amount is identical with the quantity of heat inlet.
Symmetrical in the oxidation furnace inner body wall to be provided with two baffle plates being obliquely installed, baffle plate is located under heat inlet
Side, heat inlet opening is towards baffle plate nearby, the air sent into by heat inlet, and air-flow vortex can be formed on baffle plate by beating, former
Material rotates above baffle plate to be fallen naturally again after a bit of time, makes raw material and oxygen reaction in air more abundant, plus
Fast response speed.
The setting of the oxygen tank, is to increase the oxygen concentration blasted in air in oxidation furnace, accelerate reaction speed
Rate, due to not being to blast pure oxygen, accelerates reaction rate, shortens oxidization time, production efficiency is improved again, thus
Do not increase cost overall.
The beneficial effects of the utility model：The present invention be the heat for producing electrical heating under the blowing of blower fan, by air
Together be sent to the oxygen of oxygen tank in oxidation furnace, to raw material heat supply and oxygen supply, can clean manufacturing, and can accelerate reaction
Speed, improves production efficiency；The setting of baffle plate, makes the air sent into by heat inlet, air-flow vortex can be formed on baffle plate by beating,
The oxygen in the raw material and air that fall fully is reacted, accelerate reaction rate；The setting of the oxygen tank, is to increase
The oxygen concentration in the air in oxidation furnace is blasted, accelerates reaction rate, due to not being to blast pure oxygen, reaction speed is accelerated again
Rate, shortens oxidization time, production efficiency is improved, thus does not increase cost overall.
Brief description of the drawings
Fig. 1-it is a kind of structural representation for saving oxidation unit in embodiment.
Embodiment
Below in conjunction with drawings and Examples, the utility model is described in further detail.
Reference picture 1, a kind of energy-conservation oxidation unit of the present embodiment, including oxidation furnace body 1, the oxidation furnace body 1 is from upper
And under be divided into upper furnace body 10, middle body of heater 20 and lower furnace body 30, the top of upper furnace body 10 is equipped with hopper 101, in upper furnace body 10
Interior layering is equipped with backgauge roller 103, and heat inlet 201 is left in the side of middle body of heater 20, is stretched into body of heater and connected by heat inlet 201
There is spiral thermal-collecting tube 202, some radiating air ports are left in the thermal-collecting tube 202 direction directed downwardly, directly in oxidation furnace body 1
Raw material heat supply and oxygen needed for oxidation is provided, symmetrical be provided with two gears being obliquely installed on the oxidation inwall of furnace body 1
Plate 215, baffle plate 215 is located at outside the lower section of heat inlet 201, the baffle plate 215 of the opening of heat inlet 201 direction nearby, the heat inlet 201
Face is connected with defeated heat pipe 204, and air inlet 206, the side of air inlet 206 connection oxygen are left in the lower end side of the defeated heat pipe 204
Tank 214, air inlet 206 is respectively kept with air outlet 207, air outlet by blower fan air feed with 201 or so 90 degree of direction of heat inlet
207 inner sides are equipped with retaining guard 208, and the outside of air outlet 207 connection induced duct 209, induced duct 209 leads to air-introduced machine 210, then
Lead to deduster 211, the bottom of lower furnace body 30 is connection refrigeration system 40 below discharging opening, the discharging opening, and raw material are carried out
Cooling.
The hopper 101 is equipped with the first limiter of speed 102, the refrigeration system 40 and discharging opening with the joint of upper furnace body 10
Between be provided with the second limiter of speed 213, the first limiter of speed 102 and the second limiter of speed are synchronous.
The equal subsection setup of the defeated heat pipe 204 and induced duct 209, is connected by bellows 212 between every two sections, with suitable
The change that should be expanded with heat and contract with cold, protects defeated heat pipe 204 and induced duct 209.
The outside of oxidation furnace body 1 surround wrapping using alumina silicate fiber felt, to reach the effect of insulation and sound insulation,
And fixed using four foot supports.
Mounting temperature sensor at the heat inlet 201, the outside of heat inlet 201 is connected with defeated heat by gate valve 203
Pipe 204, the gate valve 203 is controlled by temperature detect switch (TDS), and the temperature being set into stove is 450 DEG C ~ 500 DEG C, higher than 500 DEG C
Shi Zidong closing gate valves 203, during less than 450 DEG C, alarm sounds to warn.
The lower inner of defeated heat pipe 204 is equipped with electrical heating core 205, and electrical heating core 205 is entangled by defeated heat pipe 204, defeated heat
The upper end of pipe 204 respectively leads to aoxidize the heat inlet 201 of furnace body 1.
The position of the air outlet 207 interlocks up and down with the position of heat inlet 201, is conducive to airflow circulating to flow, and accelerates
Oxidation reaction.
The backgauge roller 103 is made of heat accumulation pipe, and every two layers of backgauge roller 103 is set into crisscross up and down, backgauge roller
Lateral separation is 1.5cm between 103, and heat accumulation pipe plays a part of accumulation of heat, and constantly dissipate by itself because heated and rubescent
Heat, to keep the harmony of in-furnace temperature, makes oxidation material equalization heated；The purpose that backgauge roller 103 is set be make raw material from
Hopper 101 is mutually collided when falling, and is disperseed to fall, is unlikely to rush down falling for big vast formula, and raw material can be allowed fully impartial heated
And the oxygen needed for absorption oxidation.
The oxidation furnace body 1 is cylindrical structure, and the lower furnace body 30 is in the pyramidal structure of mouth down, the upper furnace body
10 account for the 1/5 of the oxidation length of furnace body 1, and the middle body of heater 20 accounts for the 7/10 of the oxidation length of furnace body 1, and the lower furnace body 30 is grown
Degree accounts for the 1/10 of oxidation furnace body 1.
Depending on the quantity of the side heat inlet 201 of middle body of heater 20 can be according to production capacity and the length of body of heater, the air-out
The quantity of mouth 207 is identical with the quantity of heat inlet 201.
It is symmetrical on the oxidation inwall of furnace body 1 to be provided with two baffle plates being obliquely installed 215, baffle plate 215 be located at into
The hot lower section of mouth 201, the opening of heat inlet 201 is towards baffle plate 215 nearby, and the air sent into by heat inlet 201 is beaten in baffle plate
Air-flow vortex can be formed on 215, raw material are fallen naturally again after the rotation a bit of time of the top of baffle plate 215, make raw material and
Oxygen reaction in air is more abundant, accelerates reaction rate.
The setting of the oxygen tank 214, is to increase the oxygen concentration blasted in air in oxidation furnace, accelerate reaction
Speed, due to not being to blast pure oxygen, accelerates reaction rate, shortens oxidization time, production efficiency is improved again, because
And do not increase cost overall.
The utility model saves a kind of operation principle and using method of energy-conservation oxidation unit of oxidation unit：
Raw material are fallen into oxidation furnace body 1 by hopper 101, upper furnace body 10, middle body of heater are passed sequentially through from top to bottom
20 and lower furnace body 30, the oxygen of air and oxygen tank 214 is together sent to by the heat that electrical heating is produced under the blowing of blower fan
In oxidation furnace, to raw material heat supply and oxygen supply, raw material and the oxygen reaction in air in body of heater, reacted product is by system
Cooling system 40, from discharging opening discharge, the finished product after cooling, which enters, connects hexagonal reel below storage bin, storage bin, hexagonal reel is
By Motor Control, eccentric wheel is housed on motor, by a guide rod connecting eccentric wheel and hexagonal reel, makes hexagonal reel not
That stops moves back and forth, and the finished product after cooling is fallen directly on by material blanking tube in preset packaging bag or container, the sieve of hexagonal reel
Net can be exchanged according to customer demand, to meet customer need.
Claims (10)
1. one kind energy-conservation oxidation unit, including oxidation furnace body, the oxidation furnace body be divided into from top to bottom upper furnace body, middle body of heater and
Lower furnace body, it is characterised in that hopper is housed above the upper furnace body, layering is equipped with backgauge roller in upper furnace body, in middle body of heater
Side leave heat inlet, stretched into by heat inlet and thermal-collecting tube be connected with body of heater, if thermal-collecting tube direction directed downwardly is left
Symmetrical in dry radiating air port, oxidation furnace inner body wall to be provided with two baffle plates being obliquely installed, baffle plate is located at below heat inlet,
Heat inlet opening is connected with defeated heat pipe towards baffle plate nearby, the heat inlet outside, and the lower end side of the defeated heat pipe is left
Air inlet, air inlet side connection oxygen tank, dress on the inside of air outlet, air outlet is respectively kept with 90 degree of direction of heat inlet or so
There is connection induced duct outside retaining guard, air outlet, induced duct leads to air-introduced machine, then leads to deduster, and lower furnace body bottom is
Connection refrigeration system below discharging opening, the discharging opening.
2. oxidation unit is saved as claimed in claim 1, it is characterised in that the hopper is equipped with first with upper furnace body joint
Limiter of speed, is provided with the second limiter of speed between the refrigeration system and discharging opening, the first limiter of speed and the second limiter of speed are synchronous.
3. oxidation unit is saved as claimed in claim 1 or 2, it is characterised in that the defeated equal subsection setup of heat pipe and induced duct,
Connected between every two sections by bellows.
4. oxidation unit is saved as claimed in claim 1 or 2, it is characterised in that the oxidation furnace body exterior uses thermal insulation separation
Hot material is fixed around wrapping using four foot supports.
5. oxidation unit is saved as claimed in claim 1 or 2, it is characterised in that mounting temperature sensor at the heat inlet, institute
State and defeated heat pipe is connected with by gate valve outside heat inlet, the gate valve is controlled by temperature detect switch (TDS), is set into the temperature in stove
Spend for 450 DEG C ~ 500 DEG C, automatic closing gate valve during higher than 500 DEG C, during less than 450 DEG C, alarm sounds to warn.
6. oxidation unit is saved as claimed in claim 1 or 2, it is characterised in that the thermal-collecting tube is sped structure.
7. oxidation unit is saved as claimed in claim 1 or 2, it is characterised in that the defeated heat pipe lower inner is equipped with electrical heating
Core, the upper end of defeated heat pipe respectively leads to aoxidize the heat inlet of furnace body.
8. oxidation unit is saved as claimed in claim 1 or 2, it is characterised in that the position of the air outlet and the position of heat inlet
Put and interlock up and down.
9. oxidation unit is saved as claimed in claim 1 or 2, it is characterised in that the backgauge roller is made of heat accumulation pipe, every two
Layer backgauge roller is set into crisscross up and down, and lateral separation is 1.5cm between backgauge roller.
10. oxidation unit is saved as claimed in claim 1 or 2, it is characterised in that the oxidation furnace body is cylindrical structure,
The lower furnace body is in the pyramidal structure of mouth down, and the upper furnace body accounts for the 1/5 of oxidation furnace body length, and the middle body of heater accounts for oxygen
Change the 7/10 of furnace body length, the lower furnace body length accounts for the 1/10 of oxidation furnace body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621275188.1U CN206577742U (en) | 2016-11-25 | 2016-11-25 | One kind energy-conservation oxidation unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621275188.1U CN206577742U (en) | 2016-11-25 | 2016-11-25 | One kind energy-conservation oxidation unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206577742U true CN206577742U (en) | 2017-10-24 |
Family
ID=60108371
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621275188.1U Active CN206577742U (en) | 2016-11-25 | 2016-11-25 | One kind energy-conservation oxidation unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206577742U (en) |
-
2016
- 2016-11-25 CN CN201621275188.1U patent/CN206577742U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 412000 Songbai Town Songyang Village, Changning City, Hengyang City, Hunan Province Patentee after: Hunan Shuikoushan Hongwen New Material Co.,Ltd. Address before: 412000 Songbai Town Songyang Village, Changning City, Hengyang City, Hunan Province Patentee before: HUNAN SHUIKOUSHAN HONGXING CHEMICAL Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230816 Address after: 421500 Xinyuan Road, Zhupi Village, Shuikou Mountain Town, Changning City, Hengyang City, Hunan Province Patentee after: Hunan Shuikou Mountain Joint Construction New Materials Co.,Ltd. Address before: 412000 Songbai Town Songyang Village, Changning City, Hengyang City, Hunan Province Patentee before: Hunan Shuikoushan Hongwen New Material Co.,Ltd. |
|
| TR01 | Transfer of patent right |