CN204798882U - Distillation plant with filtering capability - Google Patents
Distillation plant with filtering capability Download PDFInfo
- Publication number
- CN204798882U CN204798882U CN201520505898.8U CN201520505898U CN204798882U CN 204798882 U CN204798882 U CN 204798882U CN 201520505898 U CN201520505898 U CN 201520505898U CN 204798882 U CN204798882 U CN 204798882U
- Authority
- CN
- China
- Prior art keywords
- lid
- distillation equipment
- reactor
- steam
- dispersion pipe
- 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
Abstract
The utility model provides a distillation plant with filtering capability, the distillation plant includes a cooling cylinder, the cooling cylinder includes box and lower box, evenly distributed has many condenser pipes on the inner wall of last box for the condensation of steam, go up the box with it is isolated through a lid between the box down, the middle part of box sets up a reation kettle down, reation kettle with set up a filter screen between the lid, the filter screen with the lid links to each other for filter the impurity in the steam. The distillation plant steam filtering capability has, deflector tilt up or downward sloping on the air current dispersion pipe through the structure that the dispersion was derived or disperse downwards to derive that makes progress steam, have been solved the lid and have been blockked up with stills's contact department, are equipped with the sealing washer moreover between lid and cooling cylinder, prevent the steam follow the lid with the gap department of nowel body coupling flows, and corrodes the outer wall of cooling cylinder.
Description
Technical field
The utility model relates to a kind of distillation equipment, particularly a kind of distillation equipment with filtering function.
Background technology
Distillation equipment is that to have vapo(u)rizing temperature low, and system vacuum is high, and material heated time is short, separation degree high; And separation process is irreversible, bubbling phenomenon of not seething with excitement.Outstanding being applicable to is separated higher boiling, thermal sensitivity and easily oxidized material, has been widely used in all trades and professions such as the extraction of the vitamin of pharmaceuticals industry and Chinese herbal medicine effective ingredients, petrochemical industry, food industry, cosmetics industry and agricultural.But existing distillation equipment Problems existing is, because the steam of high-temperature heating is in the middle of the process upwards walked, crystal is being produced close to the large lid between cooling cylinder and distillation still, thus block covering greatly with the contact position of distillation still, and the top of cooling cylinder due to vapor flow less than, cause inefficient problem.
Consult Chinese patent " a kind of distillation equipment ", application number: 201420519813.7, the utility model belongs to biochemical industry equipment technical field, and it relates to a kind of distillation equipment.This equipment comprises condensation chamber and distillation still, be connected by covering greatly between condensation chamber with distillation still, arranging ventilation circular hole in great Gai centre position makes condensation chamber communicate with distillation still, circular hole arranges the wireway of surrounding sealing, in the periphery of wireway, air dispersion pipe is set, the outside surrounding of air dispersion pipe arranges prerotation vane, seal cap sealing is passed through on the top of air dispersion pipe, the prerotation vane being placed in the air dispersion pipe first half is inclined upwardly, the prerotation vane being placed in air dispersion pipe Lower Half is downward-sloping, prerotation vane bottom air dispersion pipe is inclined upwardly, by steam upwards being disperseed the structure derived, solve large lid to block with the contact position of distillation still, and the top of cooling cylinder due to vapor flow less than, cause inefficient problem.
But distillation equipment described above is in steam uphill process, impurity residual in steam is followed steam and is risen together, and blocking air dispersion pipe, reduces condensation effect.
In view of above-mentioned defect, the utility model creator obtains the utility model finally through long research and practice.
Utility model content
The purpose of this utility model is, provides a kind of distillation equipment with filtering function, in order to overcome above-mentioned technological deficiency.
For achieving the above object, the technical solution adopted in the utility model is, a kind of distillation equipment with filtering function is provided, described distillation equipment comprises a cooling cylinder, described cooling cylinder comprises upper box and lower box, the inwall of described upper box is evenly distributed with many condenser pipes, in order to the condensation of steam; Cover isolated between described upper box and described lower box by one, the middle part of described lower box arranges a reactor, arranges a screen pack between described reactor and described lid, and described screen pack is connected with described lid, in order to filter the impurity in steam.
Distillation equipment described in the utility model has steam filtration function, guide plate on described air dispersion pipe is inclined upwardly or downward-sloping, by steam upwards being disperseed the structure derived or dispersion is downwards derived, solve lid to block with the contact position of distillation still, and sealing ring is provided with between lid and cooling cylinder, the gap preventing steam to be connected from described lid with described lower box is flowed out, and corrodes the outer wall of described cooling cylinder.
Preferably, described distillation equipment also comprises a heater, and described heater and described reactor are interlockingly connected.
Preferably, the upper/lower terminal face of described reactor is circular arc camber, and the upper end circular arc camber of described reactor and the middle part circular arc camber of described lid fit, and the lower end circular arc camber of described reactor and the middle part inner concave of described heater fit.
Preferably, the edge of described lid is a bent plate, and described bent plate and described lower box are interlockingly connected, and makes described lower box form an airtight space.
Preferably, described in cover an air dispersion pipe be set, the through hole covered described in described air dispersion pipe passes through is connected with described reactor.
Preferably, the sidewall of described air dispersion pipe is provided with multiple hole, a guide plate is set outside each hole, lead in order to give the steam evaporated in described reactor.
Preferably, described guide plate is one " U " type curved surface, and the described guide plate of the upper portion side wall of described air dispersion pipe is opening up, and the described guide plate of the lower sides of described air dispersion pipe is opening down.
Preferably, described reactor is arranged a wireway, described wireway stretches in described air dispersion pipe, and described air dispersion pipe and described wireway are coaxial.
Preferably, the bent plate of described lid is arranged a deflector, described deflector is about one round platform be communicated with, and the gradient of described round platform sidewall is consistent with the number of degrees of the angle between described downward opening guide plate and described air dispersion pipe, rectangular with opening up guide plate, and described guide plate is all positioned on described deflector.
Preferably, described upper box also arranges a catheter, described catheter is embedded on described upper box, and one end of described catheter is connected with described deflector, the other end is connected with a liquid reserve tank, by the drop that the inwall from described deflector and described cooling cylinder flows down, along described catheter, flow in described liquid reserve tank.
The beneficial effects of the utility model are compared with the prior art: distillation equipment described in the utility model has steam filtration function, guide plate on described air dispersion pipe is inclined upwardly or downward-sloping, by steam upwards being disperseed the structure derived or dispersion is downwards derived, solve lid to block with the contact position of distillation still, and sealing ring is provided with between lid and cooling cylinder, the gap preventing steam to be connected from described lid with described lower box is flowed out, and corrodes the outer wall of described cooling cylinder.
Accompanying drawing explanation
Fig. 1 is the structural representation that the utility model has the distillation equipment of filtering function.
Detailed description of the invention
Below in conjunction with accompanying drawing, to above-mentioned being described in more detail with other technical characteristic and advantage of the utility model.
Refer to as shown in Figure 1, it has the structural representation of the distillation equipment of filtering function for the utility model, described distillation equipment comprises a cooling cylinder 1, described cooling cylinder 1 comprises upper box 11 and lower box 12, the inwall of described upper box 11 is evenly distributed with many condenser pipes 2, in order to the condensation of steam, described lower box 12 is a hollow circular cylinder, cover 3 isolated between described upper box 11 and described lower box 12 by one, the middle part of described lid 3 is circular arc camber, the edge of described lid 3 is a bent plate 31, described bent plate 31 and described lower box 12 are interlockingly connected, and make described lower box 12 form an airtight space, the middle part of described lower box 12 arranges a reactor 4, described reactor 4 upper, lower both ends of the surface are circular arc camber, the curvature of the circular arc camber of described upper surface and the curvature of the circular arc camber of described lower surface can be the same, also can be different, the upper end curved surface of described reactor 4 and the middle part circular arc camber of described lid 3 fit, namely the curvature of the upper end curved surface of described reactor 4 is identical with the curvature of the middle part circular arc camber of described lid 3, one screen pack 5 is set between the upper end curved surface of described reactor 4 and the circular arc camber of described lid 3, described screen pack 5 is connected with described lid 3, connected mode adopts screw to connect, for convenience detach with replacing, the hole of described screen pack 5 is determined according to the particle of the material of distillation in described reactor 4, the lower end of described reactor 4 arranges a heater 6, and the middle part of described heater 6 is an inner concave, outside is a projection, described projection and described reactor 4 are interlockingly connected, the lower surface of described reactor 4 and the inner concave of described heater 6 fit, the snap fit be threaded can be adopted between described reactor 4 with described heater 6, also the mode of spring card clamping can be adopted, facilitate the dismounting between described reactor 4 and described heater 6, be convenient to the cleaning of described reactor 4, but connected mode is not limited only to above-mentioned two kinds, described lid 3 is arranged an air dispersion pipe 7, described air dispersion pipe 7 is connected with described reactor 4 by the through hole covered on 3 described in, steam in described reactor 4 is first through described screen pack 5, enter in described air dispersion pipe 7 by described circular hole again, described air dispersion pipe 7 is a hollow circular cylinder, the sidewall of described air dispersion pipe 7 is provided with multiple hole, one guide plate 8 is set outside each hole, lead in order to give the steam of evaporation in described reactor 4, described guide plate 8 is one " U " type curved surface, the guide plate 8 of the upper portion side wall of described air dispersion pipe 7 is opening up, the guide plate 8 of the lower sides of described air dispersion pipe 7 is opening down, described reactor 4 is arranged a wireway 9, described wireway 9 stretches in described air dispersion pipe 7, and described air dispersion pipe 7 is coaxial with described wireway 9, the bent plate 31 of described lid 3 is arranged a deflector 20, described deflector 20 is about one round platform be communicated with, and the gradient of described round platform sidewall is consistent with the number of degrees of the angle between described downward opening guide plate 8 and described air dispersion pipe 7, rectangular with opening up guide plate 8, the gradient of general described round platform sidewall is 45 degree, the number of degrees of the angle between described downward opening guide plate 8 and described air dispersion pipe 7 are also 45 degree, guide plate 8 on described air dispersion pipe 7 is all on described deflector 20, the steam of going out from described guide plate 8 can be made like this to run into described condenser pipe 2, be liquefied as droplet, stay along the inwall of described cooling cylinder 1 and described deflector 20, and can not enter in the gap between the inner side of described deflector 20 and described lid 3, described upper box 11 is also arranged a catheter 30, described catheter 30 is embedded on described upper box 11, and one end of described catheter 30 is connected with described deflector 20, the other end is connected with a liquid reserve tank 40, by the drop that the inwall from described deflector 20 and described cooling cylinder 1 flows down, along described catheter 30, flow in described liquid reserve tank 40, the number of described liquid reserve tank 40 can be multiple, shown in figure, the number of described liquid reserve tank 40 is two, and the symmetrical both sides being distributed in described cooling cylinder 1.
Described distillation equipment also comprises a sealing ring, and described sealing ring is arranged on the junction of described lid 3 and described lower box 12, and play the effect of sealing, the gap preventing steam to be connected from described lid 3 with described lower box 12 is flowed out.
During use, material to be distilled heats high temperature evaporation in described reactor 4, the steam formed leads to the upper box 11 of described cooling cylinder 1 by described reactor 4, steam can be filled up in space between described air dispersion pipe 7 and described wireway 9, now steam is outwards derived by described guide plate 8, in the process derived, air-flow is derived by the guide plate 8 on described air dispersion pipe 7 top obliquely, and air-flow is derived by the guide plate 8 of bottom obliquely, uniform stream is made to be dispersed in described cooling cylinder 1, and lead to rapidly on the inwall of described cooling cylinder 1, the liquid of condensation flows to described deflector 20 on the inwall of described cooling cylinder 1, by described catheter 30, finally enter in described liquid reserve tank 40.
Distillation equipment described in the utility model has steam filtration function, guide plate on described air dispersion pipe is inclined upwardly or downward-sloping, by steam upwards being disperseed the structure derived or dispersion is downwards derived, solve lid to block with the contact position of distillation still, and sealing ring is provided with between lid and cooling cylinder, the gap preventing steam to be connected from described lid with described lower box is flowed out, and corrodes the outer wall of described cooling cylinder.
The foregoing is only preferred embodiment of the present utility model, is only illustrative for the utility model, and nonrestrictive.Those skilled in the art is understood, and can carry out many changes in the spirit and scope that the utility model claim limits to it, amendment, even equivalence, but all will fall in protection domain of the present utility model.
Claims (10)
1. have a distillation equipment for filtering function, it is characterized in that, described distillation equipment comprises a cooling cylinder, and described cooling cylinder comprises upper box and lower box, the inwall of described upper box is evenly distributed with many condenser pipes, in order to the condensation of steam; Cover isolated between described upper box and described lower box by one, the middle part of described lower box arranges a reactor, arranges a screen pack between described reactor and described lid, and described screen pack is connected with described lid, in order to filter the impurity in steam.
2. distillation equipment according to claim 1, is characterized in that, described distillation equipment also comprises a heater, and described heater and described reactor are interlockingly connected.
3. distillation equipment according to claim 2, it is characterized in that, the upper/lower terminal face of described reactor is circular arc camber, the upper end circular arc camber of described reactor and the middle part circular arc camber of described lid fit, and the lower end circular arc camber of described reactor and the middle part inner concave of described heater fit.
4. distillation equipment according to claim 3, is characterized in that, the edge of described lid is a bent plate, and described bent plate and described lower box are interlockingly connected, and makes described lower box form an airtight space.
5. distillation equipment according to claim 4, is characterized in that, described in cover an air dispersion pipe be set, the through hole covered described in described air dispersion pipe passes through is connected with described reactor.
6. distillation equipment according to claim 5, is characterized in that, the sidewall of described air dispersion pipe is provided with multiple hole, arranges a guide plate outside each hole, leads in order to give the steam evaporated in described reactor.
7. distillation equipment according to claim 6, is characterized in that, described guide plate is one " U " type curved surface, and the described guide plate of the upper portion side wall of described air dispersion pipe is opening up, and the described guide plate of the lower sides of described air dispersion pipe is opening down.
8. distillation equipment according to claim 7, is characterized in that, described reactor is arranged a wireway, and described wireway stretches in described air dispersion pipe, and described air dispersion pipe and described wireway are coaxial.
9. distillation equipment according to claim 8, it is characterized in that, the bent plate of described lid is arranged a deflector, described deflector is about one round platform be communicated with, and the gradient of described round platform sidewall is consistent with the number of degrees of the angle between described downward opening guide plate and described air dispersion pipe, rectangular with opening up guide plate, and described guide plate is all positioned on described deflector.
10. distillation equipment according to claim 9, it is characterized in that, described upper box also arranges a catheter, described catheter is embedded on described upper box, and one end of described catheter is connected with described deflector, the other end is connected with a liquid reserve tank, by the drop that the inwall from described deflector and described cooling cylinder flows down, along described catheter, flow in described liquid reserve tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520505898.8U CN204798882U (en) | 2015-07-13 | 2015-07-13 | Distillation plant with filtering capability |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520505898.8U CN204798882U (en) | 2015-07-13 | 2015-07-13 | Distillation plant with filtering capability |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204798882U true CN204798882U (en) | 2015-11-25 |
Family
ID=54583775
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520505898.8U Expired - Fee Related CN204798882U (en) | 2015-07-13 | 2015-07-13 | Distillation plant with filtering capability |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204798882U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107228778A (en) * | 2017-07-28 | 2017-10-03 | 洛阳市三诺化工有限公司 | A kind of sampling rectifier unit of TBP tributyl phosphates |
| CN107376391A (en) * | 2017-07-19 | 2017-11-24 | 浙江全世科技有限公司 | Automatic feed liquor control device and method for dual distillation equipment |
| CN108607267A (en) * | 2018-05-11 | 2018-10-02 | 成都斯力康科技股份有限公司 | A kind of recovery processing technique and its processing unit of organosilicon slag slurry |
-
2015
- 2015-07-13 CN CN201520505898.8U patent/CN204798882U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107376391A (en) * | 2017-07-19 | 2017-11-24 | 浙江全世科技有限公司 | Automatic feed liquor control device and method for dual distillation equipment |
| CN107228778A (en) * | 2017-07-28 | 2017-10-03 | 洛阳市三诺化工有限公司 | A kind of sampling rectifier unit of TBP tributyl phosphates |
| CN108607267A (en) * | 2018-05-11 | 2018-10-02 | 成都斯力康科技股份有限公司 | A kind of recovery processing technique and its processing unit of organosilicon slag slurry |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204798882U (en) | Distillation plant with filtering capability | |
| CN204147570U (en) | A kind of distillation equipment | |
| CN103143184B (en) | Distillation apparatus | |
| CN205699523U (en) | One may filter that efficient distillation equipment | |
| CN205718530U (en) | A kind of fractional condensaion dish structure being applicable to vacuum distilling | |
| CN204319793U (en) | A kind of efficient energy-saving economic benefits and social benefits external circulation evaporator | |
| CN206867751U (en) | A kind of eucalyptus oil classification rectifier unit that can adjust temperature | |
| CN206315497U (en) | A kind of cooling driers air cleaner | |
| CN210432784U (en) | Honey processing is with equipment of dehydration | |
| CN208611814U (en) | A kind of falling film type film evaporator | |
| CN206089622U (en) | High accuracy flower bud of lily magnolia flower extraction of essential oil device | |
| CN208406128U (en) | The double-deck material filling type packed tower | |
| CN208031952U (en) | A kind of natural extract rectifier unit of desalination senile plaque | |
| CN205287661U (en) | Trace liquid distillation plant | |
| CN208726782U (en) | A kind of cracking oil product divides oil cooler | |
| CN205379681U (en) | Highly enriched extrinsic cycle MVR evaporimeter | |
| CN208511890U (en) | A kind of continuous device for removing low-boiling-point substance in flowing material | |
| CN208493276U (en) | A kind of condensing plant and liquor production system | |
| CN208250270U (en) | One kind using wine distillation equipment for red hayberry wine processing purification | |
| CN204193738U (en) | A kind of volatile organic solvent condensate recycling device | |
| CN208553184U (en) | Packed tower barrel structure and stuffing rectification column | |
| CN106731419A (en) | A kind of gas recovery system for oil and method | |
| CN113476871A (en) | Multi-effect evaporation control process for one-time tank passing by self pressure difference | |
| CN209307319U (en) | A kind of extraction plants essential oil freezing and heating alternately equipment | |
| CN207734636U (en) | A kind of temperature with high efficiency cold-trap |
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 |
Granted publication date: 20151125 Termination date: 20160713 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |