CN205838584U - The silicon dioxide hydrolysis stove of tangential counter-flow heat exchange - Google Patents
The silicon dioxide hydrolysis stove of tangential counter-flow heat exchange Download PDFInfo
- Publication number
- CN205838584U CN205838584U CN201620261500.5U CN201620261500U CN205838584U CN 205838584 U CN205838584 U CN 205838584U CN 201620261500 U CN201620261500 U CN 201620261500U CN 205838584 U CN205838584 U CN 205838584U
- Authority
- CN
- China
- Prior art keywords
- cooling tube
- heater
- bell
- heat exchange
- silicon dioxide
- 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.)
- Expired - Fee Related
Links
Landscapes
- Silicon Compounds (AREA)
Abstract
The silicon dioxide hydrolysis stove of a kind of tangential counter-flow heat exchange of this utility model, including body of heater, the top of body of heater has the bell being tightly connected, bell and bottom of furnace body to be all the structure of truncated cone face shape；Having spiral helicine cooling tube in body of heater, the upper end of cooling tube is tightly connected with the feed pipe being connected on bell, and the lower end of cooling tube and the discharge nozzle being connected to bottom of furnace body are tightly connected；Bottom of furnace body has and prolongs tangentially connected air inlet pipe joint, have on bell and prolong tangentially connected escape pipe joint, so-called tangentially connected, refer to that the side of pipe joint is tangent with described truncated cone face be connected, and the angle of the axis of pipe joint and body of heater centrage is equal to the helical angle of the helicoidal structure of cooling tube.This utility model has countercurrent flow, the time extending heat exchange cooling, avoids high-speed gas kinetic energy rejection, makes hot fluid cool down most effectively, is beneficial to the silicon dioxide hydrolysis advantage such as stove miniaturization.
Description
Technical field
This utility model belongs to silicon dioxide hydrolysis stove technical field, is specifically related to a kind of silicon dioxide aerosol
Chiller.
Background technology
Silicon dioxide hydrolysis stove is one of topmost equipment in silicon dioxide producing device.From nozzle reaction with
After aerosol under the effect of negative pressure from top to bottom enter hydrolysis stove, in body of heater through with as cooling
After the air heat-exchange of medium, flow out from the discharging opening of bottom of furnace body, aerosol be minimized temperature to adapt to after
The technological requirement of continuous operation.
The hydrolysis stove of prior art, owing to structure configuration is not reasonable so that containing the heat of mixing of silicon dioxide
Gas can not be sufficiently cool, it is impossible to meets and produces needs, on the other hand there is also cooling gas and the wave of time
Take, add production cost.
Such as Chinese patent ZL 201420489689.4, the practicality of entitled " silicon dioxide hydrolysis stove " is new
Type patent, open a kind of silicon dioxide hydrolysis furnace structure of knowing clearly, including the body of heater of jacketed, the material of this body of heater
Entrance is for cutting sth. askew to entrance, and the entrance of chuck, for cutting sth. askew to entrance, is cut sth. askew to the most right for two.The height of this patent
Temperature silicon dioxide aerosol enter from the top of body of heater body of heater with the cooling air heat-exchange entered chuck, but
It is that its body of heater cavity is in the most through structure so that high temperature silica aerosol the most only flows through
The extremely short time, then the most directly filling and let out furnace bottom outflow, the structure of this heat exchange causes high temperature titanium dioxide
Silicon aerosol is short owing to spending the stream time in body of heater, adds that its heat exchange area is little, so heat transfer effect is poor, high
Temperature silicon dioxide aerosol can not cool to required temperature.
Summary of the invention
Technical problem to be solved in the utility model is, overcomes the silicon dioxide hydrolysis stove of prior art to exist
High temperature silica aerosol to spend the stream time short, heat exchange area is little, the defect of heat transfer effect difference, it is provided that
Planted the silicon dioxide hydrolysis stove that the stream time is longer, heat exchange area is relatively big, lowered the temperature.
The purpose of this utility model is achieved by following technical proposals: a kind of tangential counter-flow heat exchange
Silicon dioxide hydrolysis stove, including body of heater, the bell being tightly connected, bell and body of heater are arranged at the top of body of heater
Bottom is all the structure of truncated cone face shape；Body of heater has spiral helicine cooling tube, the upper end of cooling tube and company
The feed pipe being connected on bell is tightly connected, and the lower end of cooling tube and the discharge nozzle being connected to bottom of furnace body seal
Connect；Bottom of furnace body has and prolongs tangentially connected air inlet pipe joint, bell has and prolongs tangentially connected escape pipe and connect
Head, so-called tangentially connected, refer to that the side of pipe joint is tangent with described truncated cone face and be connected, and pipe joint
The angle of axis and body of heater centrage equal to the helical angle of the helicoidal structure of cooling tube.
Counter-flow heat exchange is called for short countercurrent flow, as follows.
Silicon dioxide aerosol prolongs cooling Bottomhole pressure from top to bottom, cooling medium, and i.e. cooling air is from lower
On in the flows outside of cooling tube, both become countercurrent flow relation to configure, and the advantage of countercurrent flow is to work as bar
When part is identical, the logarithmic mean temperature difference (LMTD) of countercurrent flow is all bigger than other all of heat exchange modes, and especially ratio is suitable
Stream heat exchange is much greater, and countercurrent flow can make hot fluid cool down most effectively.
Cooling tube is arranged by helical form, greatly extends the distance that silicon dioxide aerosol flows through, Ye Jiyan
Grow the time of heat exchange cooling, in other words, for same heat transfer effect, so that it may the structure making body of heater is tighter
Gather, volume smallerization of body of heater.
Cooling tube is arranged by helical form, the high temperature fluid of crooked position flowing in spiral helicine cooling tube, its
Flow velocity near kernel of section position fluid is less than the flow velocity of the fluid near cross section outside left, if slightly disturbing
Dynamic, easily form turbulence effects, in other words, lateral fluid hybrid switching in being formed, this is for higher temperature
Fluid flow to wall with improve heat transfer effect be highly advantageous.
Prolong tangentially connected air inlet pipe joint, it is to avoid kinetic energy rejection is caused in Fast Cooling gas direct collision furnace wall,
And make cooling fluid be prolonged diagonal upward direction spiral flow by face, furnace wall guiding, i.e. expand and described serpentine pipe
Time of contact, improve heat exchange efficiency.
Preferred version, feed pipe prolongs and is tangentially connected with bell, and discharge nozzle prolongs and is tangentially connected with bottom of furnace body.
Preferred version, cooling tube is parallel with 2-3 root.
Preferred version, the cooling tube of described 2-3 root parallel connection is pressed point intervals such as multiple start thread form and is arranged.
The beneficial effects of the utility model are:
1, countercurrent flow can make hot fluid cool down most effectively；
2, drastically increase the distance that silicon dioxide aerosol flows through, namely extend the time that heat exchange cools down,
More compact structure and the miniaturization of body of heater can be made；
3, form turbulence effects in being beneficial to cooling tube, improve heat transfer effect；
4, tangentially connected air inlet pipe joint, it is to avoid high-speed gas kinetic energy rejection, and make cooling fluid by furnace wall
Face guides prolongs diagonal upward direction spiral flow, improves heat exchange efficiency.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of embodiment of this utility model.
In figure, body of heater 1；Bottom of furnace body 11；Bell 2；Cooling tube 3；Feed pipe 4；Discharge nozzle 5；Enter
Gas-tpe fitting 6；Escape pipe joint 7.
Detailed description of the invention
With specific embodiments, this utility model is further described below in conjunction with the accompanying drawings.
Embodiment 1: as it is shown in figure 1, the silicon dioxide hydrolysis stove of a kind of tangential counter-flow heat exchange, including body of heater
1, the top of body of heater 1 has the bell 2 being tightly connected, bell 2 and bottom of furnace body 11 to be all truncated cone face shape
The structure of shape；Body of heater 1 has spiral helicine cooling tube 3, the upper end of cooling tube 3 be connected on bell 1
Feed pipe 4 is tightly connected, and the lower end of cooling tube 3 and the discharge nozzle 5 being connected to bottom of furnace body 11 are tightly connected；
The air inlet pipe joint 6 that bottom of furnace body 11 side of truncated cone face shape and structure has direction to be tangential fixing connection,
Having direction on bell 2 is to prolong tangentially connected escape pipe joint 7, mentioned here tangentially connected, refers to air inlet
Pipe joint 6 or escape pipe joint 7 pass through mutually with described truncated cone face and are connected, and air inlet pipe joint 6 or give vent to anger
The side of pipe joint 7 is tangent with described truncated cone face to be connected, air inlet pipe joint 6 or escape pipe joint 7 simultaneously
The angle of axis and body of heater 1 centrage equal to the helical angle of the helicoidal structure of cooling tube 3, also want for this
The half seeking the cone angle in described truncated cone face will be with described helical angle complementary angle each other.Feed pipe 4 along tangential with
Bell 2 connects, and discharge nozzle 5 is along being tangentially connected with bottom of furnace body 11.
During work, high temperature silica aerosol prolongs flowing in cooling tube 3 from top to bottom, and cooling air is from entering
Gas-tpe fitting 6 enters body of heater 1.And from bottom to top in the flows outside of cooling tube 3, high temperature silica gas is molten
Glue becomes countercurrent flow relation to configure with cooling air, and the advantage of countercurrent flow is, when condition is identical,
The logarithmic mean temperature difference (LMTD) of countercurrent flow is all bigger than other all of heat exchange modes, especially big than following current heat exchange
Much；Countercurrent flow can make hot fluid cool down most effectively.
Cooling tube 3 is arranged by helical form, drastically increases the distance that silicon dioxide aerosol flows through, namely
Extend the time of heat exchange cooling, in other words, for same heat transfer effect, so that it may make the structure of body of heater more
Compact, volume smallerization of body of heater.
And, cooling tube 3 is arranged by helical form, the high temperature of crooked position flowing in spiral helicine cooling tube
Fluid, its flow velocity near kernel of section position is different, easily with the rate of flow of fluid near cross section outside left
In being formed, lateral fluid is disturbed moves and hybrid switching, even forms turbulence effects, and this is for the stream of higher temperature
It is highly advantageous that direction of flow wall improves heat transfer effect.
Air inlet pipe joint 6 prolongs tangentially connected, it is to avoid kinetic energy rejection is caused in high-speed gas direct collision furnace wall, and
Make cooling fluid be guided by face, furnace wall and prolong diagonal upward direction spiral flow, i.e. expand and the connecing of described serpentine pipe
The time of touching, improve heat exchange efficiency.
Embodiment 2: the cooling tube that the pyramid type serpentine pipe that the hand of spiral is identical is constituted, has 2, and 2 cold
But pipe staggers 180 ° along the circumference of body of heater, then the upper end of 2 cooling tubes is in parallel, then by transition conduit
It is tightly connected with the feed pipe being connected on bell；Equally, the lower end of 2 cooling tubes is in parallel by transition conduit,
Then it is tightly connected with the discharge nozzle being connected to bottom of furnace body.Remaining structure is with embodiment 1.
This utility model be applicable to silicon dioxide hydrolysis stove, have countercurrent flow, extend heat exchange cooling time,
Turbulence effects, tangentially connected air inlet pipe joint all it is easily formed outside pipe inner tube, it is to avoid high-speed gas kinetic energy rejection,
Make hot fluid cool down most effectively, be beneficial to the advantages such as miniaturization.If those skilled in the art is to above-mentioned
Bright content is made simple amendment or replaces, and such change is not to be regarded as a departure from scope of the present utility model,
All so obvious to those skilled in the art amendments are included within right of the present utility model and want
Within the scope of asking.
Claims (4)
1. the silicon dioxide hydrolysis stove of tangential counter-flow heat exchange, including body of heater, the top of body of heater is tightly connected
Bell, it is characterized in that, bell and bottom of furnace body are all the structure of truncated cone face shape；Body of heater has spiral shell
The cooling tube of rotation shape, the upper end of cooling tube is tightly connected with the feed pipe being connected on bell, under cooling tube
End is tightly connected with the discharge nozzle being connected to bottom of furnace body；Bottom of furnace body has and prolongs tangentially connected air inlet pipe joint,
Have on bell and prolong tangentially connected escape pipe joint, so-called tangentially connected, refer to that the side of pipe joint is with described
The tangent connection in truncated cone face, and the angle of the axis of pipe joint and body of heater centrage is equal to the spiral of cooling tube
The helical angle of shape structure.
The silicon dioxide hydrolysis stove of tangential counter-flow heat exchange the most according to claim 1, is characterized in that,
Feed pipe prolongs and is tangentially connected with bell, and discharge nozzle prolongs and is tangentially connected with bottom of furnace body.
The silicon dioxide hydrolysis stove of tangential counter-flow heat exchange the most according to claim 1 and 2, its feature
It is that cooling tube is parallel with 2-3 root.
The silicon dioxide hydrolysis stove of tangential counter-flow heat exchange the most according to claim 3, is characterized in that,
The cooling tube of described 2-3 root parallel connection is pressed point intervals such as multiple start thread form and is arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620261500.5U CN205838584U (en) | 2016-03-31 | 2016-03-31 | The silicon dioxide hydrolysis stove of tangential counter-flow heat exchange |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620261500.5U CN205838584U (en) | 2016-03-31 | 2016-03-31 | The silicon dioxide hydrolysis stove of tangential counter-flow heat exchange |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205838584U true CN205838584U (en) | 2016-12-28 |
Family
ID=57627491
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620261500.5U Expired - Fee Related CN205838584U (en) | 2016-03-31 | 2016-03-31 | The silicon dioxide hydrolysis stove of tangential counter-flow heat exchange |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205838584U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107152873A (en) * | 2017-06-01 | 2017-09-12 | 无锡市必盛水处理剂有限公司 | One kind production sodium metasilicate cooling conveying device |
| CN109012523A (en) * | 2018-08-02 | 2018-12-18 | 安徽海蚨祥橡胶有限公司 | A kind of silica hydrolysis furnace for the production of rubber-plastic sealing part |
| CN112461017A (en) * | 2020-11-13 | 2021-03-09 | 浙江启尔机电技术有限公司 | Thermal buffer tank, liquid supply device using the same and thermal buffer method |
-
2016
- 2016-03-31 CN CN201620261500.5U patent/CN205838584U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107152873A (en) * | 2017-06-01 | 2017-09-12 | 无锡市必盛水处理剂有限公司 | One kind production sodium metasilicate cooling conveying device |
| CN109012523A (en) * | 2018-08-02 | 2018-12-18 | 安徽海蚨祥橡胶有限公司 | A kind of silica hydrolysis furnace for the production of rubber-plastic sealing part |
| CN112461017A (en) * | 2020-11-13 | 2021-03-09 | 浙江启尔机电技术有限公司 | Thermal buffer tank, liquid supply device using the same and thermal buffer method |
| CN112461017B (en) * | 2020-11-13 | 2022-08-30 | 浙江启尔机电技术有限公司 | Thermal buffer tank, liquid supply device using the same, and thermal buffer method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205838584U (en) | The silicon dioxide hydrolysis stove of tangential counter-flow heat exchange | |
| CN106679467B (en) | Shell-and-tube heat exchanger with external bobbin carriage | |
| CN105890405B (en) | A kind of dual grooved strengthens tube type heat exchangers | |
| CN105937857B (en) | A kind of shell-and-tube heat exchanger being suitable for three fluid heat transfers | |
| CN205808180U (en) | A kind of shell-and-tube heat exchanger being applicable to three fluid heat transfers | |
| CN203253440U (en) | Conical spiral pipe type jet reactor | |
| CN101162129B (en) | Method for utilizing cracking gas waste heat and gas-gas exchanger used therefor | |
| CN106542730A (en) | A kind of chiller | |
| CN205856011U (en) | It is provided with the silicon dioxide hydrolysis stove of spiral type heat exchange runner | |
| CN206626991U (en) | A kind of close-coupled micro-channel heat exchanger | |
| CN202915742U (en) | Tangential continuous spiral diversion winding pipe condenser | |
| CN201748715U (en) | Finned tube type heat exchanger | |
| CN209797487U (en) | Oxygen and ozone mixed gas separation device | |
| CN212548369U (en) | Regenerated gas separator | |
| CN204495076U (en) | A kind of high-temperature calcination stove petroleum coke cooling jacket | |
| CN208333176U (en) | Flow heat exchanger | |
| CN203240927U (en) | Conical heat exchanger | |
| CN209230039U (en) | A kind of integrally formed vaporation-type solar thermal collector | |
| CN207313155U (en) | Aoxidize zinc recovering cooling device | |
| CN106052416B (en) | A kind of injection mould cooling tower | |
| CN207214863U (en) | Bushing type micro-channel heat exchanger | |
| CN206774253U (en) | Containment built-in heat exchanger | |
| CN105333614B (en) | Heat-pump water-heater water tank | |
| CN201512491U (en) | Novel inner-cooling stop tube of PVC polymeric kettle | |
| CN104879970B (en) | A kind of double centrifugation flash vessels of emptying structure changes |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161228 Termination date: 20190331 |