CN206008077U - The distillating still of feeding can be facilitated - Google Patents
The distillating still of feeding can be facilitated Download PDFInfo
- Publication number
- CN206008077U CN206008077U CN201620967659.9U CN201620967659U CN206008077U CN 206008077 U CN206008077 U CN 206008077U CN 201620967659 U CN201620967659 U CN 201620967659U CN 206008077 U CN206008077 U CN 206008077U
- Authority
- CN
- China
- Prior art keywords
- distillating still
- valve
- air inlet
- tube
- probe tube
- 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
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model discloses a kind of distillating still, including distillating still body, charging aperture is set at the top of distillating still body, feed pipe is set at charging aperture, its bottom arranges discharge gate, discharge gate connects drainage conduit, air inlet is also set up in distillating still bottom, and described air inlet connection conveys the air inlet pipe of vapor, the discharge for making feedstock vapor escape is additionally provided with distillating still body top, also include probe tube, caliber of the caliber of probe tube described in the probe tube less than drainage conduit；One end of probe tube is arranged on transverse tube, and the other end is upwardly extended, and is arranged elbow in its end, is arranged the first valve and the second valve in drainage conduit.This utility model compared with prior art, which increases caliber less probe tube and chemical industry bed material is sampled, and the flow of chemical industry bed material is significantly controlled, and chemical industry bed material is released automatically, and without the need for manually take, security performance has ensured.
Description
Technical field
This utility model is related to a kind of chemical production equipment, specifically, is a kind of distillating still.
Background technology
Distillating still be in Chemical Manufacture commonly use reaction utensil, its chemical industry bed material in kettle is carried out using water vapour plus
Heat, and then the steam of industrial chemicals is produced, industrial chemicals steam is input into material collection device by discharge.Distilling
Need to be monitored the progress that distills in real time in journey, i.e., the chemical industry bed material in regularly needing to distillating still is sampled, tradition
Distillating still sample when need open bottom discharge gate, to discharge chemicals bed material carry out concentration analysis, so as to obtain
The progress of distillation.In general, all than larger, can cause during sampling substantial amounts of to ensure the speed of discharge, drainage conduit caliber
Bed material is released, and the waste for causing resource of certainty, the method for only controlling its flow manually by slight Open valve are entered
Row sampling, and control that its subjectivity is larger manually, flow can not be controlled very precisely.And distillation work must be stopped by sampling work
Can carry out after only, what which was invisible extends the time of work, and in still-process can produce substantial amounts of heat, if cooling is not filled
Divide and be then easy to be burned in sampling process.Huge hidden danger is caused to the personal safety of operator.
Content of the invention
The purpose of this utility model is to provide a kind of wasting of resources few, safe distillating still.
This utility model is realized using following technological means：One kind can facilitate feeding distillating still, including distillating still sheet
Body, arranges charging aperture at the top of distillating still body, arranges feed pipe at charging aperture, and its bottom arranges discharge gate, and discharge gate connects
Run in expects pipe, drainage conduit is divided into straight tube and transverse tube, and transverse tube is connected with each other with one end of straight tube, the other end connection of transverse tube is filtered
Groove, also sets up air inlet in distillating still bottom, and described air inlet connection conveys the air inlet pipe of vapor, on distillating still body top
End is additionally provided with the discharge for making feedstock vapor escape, and also includes probe tube, and described in the probe tube, the caliber of probe tube is less than
The caliber of drainage conduit；
Described probe tube is L-type pipe, and the horizontal ends of L-type pipe are connected on the straight tube of drainage conduit.The end of vertical end sets
Put elbow, the second valve be arranged on transverse tube near with the position of straight tube junction on；
Air intake branch is also set up in air inlet pipe, and one end of described air intake branch connects air inlet pipe, and the other end stretches into steaming
The top of kettle body is evaporated, the 3rd valve is set on air intake branch, in the air inlet pipe of air intake branch Yu air inlet pipe junction bottom
The 4th valve of upper setting.
Also include that heat reclaim unit, described heat reclaim unit include condenser and escape pipe, one end of condenser
Connection discharge, the other end connect one end of escape pipe, and the other end connection material collection device of escape pipe is set on discharge
Put the 5th valve.
Control device, the remotely controlled case control of control device are set on described valve.
This utility model compared with prior art, which increases caliber less probe tube and chemical industry bed material is taken
Sample, the flow of chemical industry bed material are significantly controlled, and chemical industry bed material is released automatically, without the need for manually taking, safety
Can ensure, this utility model also sets up heat reclaim unit and carries out the recovery of heat to industrial chemicals steam, which achieves
The circulation of the energy, so that avoid the waste of the energy.
Description of the drawings
Fig. 1 is this utility model structural representation.
Wherein 1- distillating stills body, 2- drainage conduits, the first valves of 3-, 4- probe tubes, 5- air inlet pipe, 6- air intake branches, 7-
3rd valve, the 4th valves of 8-, 9- discharges, 10- condensers, 11- escape pipes, the 5th valves of 12-, the second valves of 13-.
Specific embodiment
This utility model is described in further detail with reference to Figure of description：
This utility model relate to a kind of distillating still, and which includes a distillating still body 1, at the top of distillating still body 1
And bottom, charging aperture and discharge gate is respectively provided with, feed pipe is set at charging aperture, drainage conduit 2 is set at discharge gate, steamed
The bottom for evaporating kettle also sets up air inlet, and air inlet connection conveys the air inlet pipe 5 of vapor, and top also sets up collection QI KOU, in gas collection
Discharge 9 is set on mouth, and chemical industry bed material is put in distillating still body by charging aperture, then passes through 5 inside input water of air inlet pipe
Steam is distilled to which, is distilled the industrial chemicals steam for obtaining and is transferred out by discharge 9, distills remaining material residue
Outside distillating still body is discharged by drainage conduit 2, complete distillation action is completed once.
In this utility model, described distillating still also includes that a probe tube 4, probe tube 4 are set to L-type, and described takes
Sample pipe 4 is arranged on vertical tube, and the horizontal ends of probe tube are connected with vertical tube, arranges elbow, the elbow in the end of its vertical end
Direction facing away from distillating still body, and can arbitrarily adjust in the range of 180 °.In this utility model, described probe tube 4
Caliber of the caliber less than transverse tube, specifically, between 3-5cm, in its unit interval, flow is constant, i.e., for the caliber of probe tube 4
Just every time Open valve when open that size is different, which still can guarantee that the maximum of flows per unit time, make the user will not be by
Scald.
In this utility model, valve is set in described drainage conduit, specifically, valve arranges 2, is divided into the first valve
Door 3 and the second valve 13, the first valve 3 are arranged on vertical tube, and the second valve 13 is arranged on transverse tube, specifically, described
Second valve 13 is arranged on transverse tube near the adjacent one end with vertical tube junction, its object is to timely block in transverse tube and flows
Bed material, make which rapidly enter in probe tube 4.
Drainage conduit 2 is arranged on the downside of vertical tube, also can be in same level with transverse tube, if being in same level,
Then the junction of transverse tube and vertical tube arranges threeway, arranges a connecting tube in the junction of threeway and probe tube, and the two of connecting tube
Port footpath is adapted with threeway and probe tube respectively
This utility model also includes that an air intake branch 6, one end of air intake branch 6 are arranged in air inlet pipe 5, and the other end is stretched
Enter in distillating still body 1, specifically, air intake branch 6 stretches into the top of distillating still body 1, the 3rd is arranged on air intake branch 6
Valve 7, arranges the 4th valve 8 in air inlet pipe, and specifically, the 4th valve 8 is arranged on the bottom of air inlet pipe 5, more specific next
Say, be arranged on the bottom of air intake branch 6 and 5 junction of air inlet pipe.
This utility model also includes that a heat reclaim unit, the heat reclaim unit are arranged on discharge 9, and which wraps
A condenser 10 and an escape pipe 11 is included, one end of condenser 10 is arranged on the end of discharge 9, and the other end connects outlet
One end of pipe 11, arranges water inlet and outlet on condenser, and water inlet is connected a water circulating pump, recirculated water with outlet
Pump connect a hot-water cylinder, by condenser in water constantly circulate, by flow into condenser in industrial chemicals steam carry out cold
But, stored in cooling water input hot-water cylinder, then heated water is sent into and produces vapor, realize energy
The recycling of amount, arranges the 5th valve 12 on discharge 9 in this utility model.
Condenser described in the utility model also directly can be socketed on discharge 9, in condenser arrange spiral element
Road is used for conveying condensed water.The caliber of described serpentine pipe equal with the caliber of discharge 9 or be slightly larger than its caliber, such one
Come, the heat of chemical industry feedstock vapor just can be fully absorbed in discharge 9, more save energy.
In order to ensure the safety of operator, which can arrange control device at valve, be carried out using control chamber long-range
Control, specifically, exactly assigns instruction by control chamber, makes opening and closing and the opening angle of control device operation valve, so as to
Order operation is safer, also more accurate.
Describe in detail below by a specific example：
During distillation process is carried out, the first valve closing, the second valve are also switched off, and the 3rd valve opens conveying water
Steam, the 4th valve closing, the 5th valve open release chemical raw material vapour, once need to sample, then by the 3rd valve closing,
4th valve is opened, the 5th valve is also switched off, while opening the 4th valve carries out vapor output from upper end, open the first valve
Door, due to vapor, constantly conveying causes pressure increase in kettle, and under pressure, chemical industry bed material is extruded from probe tube, real
Now sample；After sampling is finished, the first valve and the 4th valve is closed, open the 3rd valve and proceed to give birth to the 5th valve
Produce.When distillation completes discharging, by the 3rd valve and the 5th valve closing, opening the first valve and the second valve carries out discharging,
Due to probe tube different from drainage conduit caliber, and in kettle pressure also less, therefore bed material will not be spilt from probe tube.
Claims (3)
1. a kind of distillating still for facilitating feeding, including distillating still body, arranges charging aperture, charging at the top of distillating still body
Mouthful place arranges feed pipe, and its bottom arranges discharge gate, and discharge gate connects drainage conduit, and drainage conduit is divided into straight tube and transverse tube, transverse tube and
One end of straight tube is connected with each other, the other end connection filter tank of transverse tube, also sets up air inlet, described air inlet in distillating still bottom
The air inlet pipe of mouth connection conveying vapor, is additionally provided with the discharge for making feedstock vapor escape on distillating still body top, and which is special
Levy and be：Also include probe tube, caliber of the caliber of probe tube described in the probe tube less than drainage conduit；
Described probe tube is L-type pipe, and the horizontal ends of L-type pipe are connected on the straight tube of drainage conduit, and the end of vertical end arranges curved
Head, the second valve be arranged on transverse tube near with the position of straight tube junction on；
Air intake branch is also set up in air inlet pipe, and one end of described air intake branch connects air inlet pipe, and the other end stretches into distillating still
The top of body, on air intake branch arranges the 3rd valve, sets in the air inlet pipe of air intake branch with air inlet pipe junction bottom
Put the 4th valve.
2. distillating still according to claim 1, it is characterised in that：Also include heat reclaim unit, described heat recovery
Device includes that condenser and escape pipe, one end connection discharge of condenser, the other end connect one end of escape pipe, escape pipe
The other end connects material collection device, arranges the 5th valve on discharge.
3. distillating still according to claim 1, it is characterised in that：Control device, control device are set on described valve
Remotely controlled case control.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620967659.9U CN206008077U (en) | 2016-08-26 | 2016-08-26 | The distillating still of feeding can be facilitated |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620967659.9U CN206008077U (en) | 2016-08-26 | 2016-08-26 | The distillating still of feeding can be facilitated |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206008077U true CN206008077U (en) | 2017-03-15 |
Family
ID=58254386
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620967659.9U Expired - Fee Related CN206008077U (en) | 2016-08-26 | 2016-08-26 | The distillating still of feeding can be facilitated |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206008077U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109621474A (en) * | 2018-12-27 | 2019-04-16 | 昆山城东化工有限公司 | A kind of multistage cooling recovery system for organic solvent of automatic control |
-
2016
- 2016-08-26 CN CN201620967659.9U patent/CN206008077U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109621474A (en) * | 2018-12-27 | 2019-04-16 | 昆山城东化工有限公司 | A kind of multistage cooling recovery system for organic solvent of automatic control |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105413204B (en) | Thermal cycle machinery Compression Evaporation device and the method that zinc sulfate is prepared using the device | |
| CN206008077U (en) | The distillating still of feeding can be facilitated | |
| CN105664801A (en) | Gas/liquid switching feeding device and heavy organic matter pyrolysis device | |
| CN206127267U (en) | Distillation plant of making wine usefulness | |
| CN101966396B (en) | Evaporation device | |
| CN206008056U (en) | A kind of distillating still that conveniently can be sampled | |
| CN106969953A (en) | The device for making and its oxidizing fire method of a kind of organic tritium carbon sample | |
| CN204101354U (en) | Dry coke quenching and coke-oven gas analyze sample Flash Gas Compression Skid System | |
| CN104891766B (en) | Sludge pyrohydrolysis device and method | |
| CN107062865A (en) | A kind of continuous drying system | |
| CN107034011B (en) | Continuous preparation method of cinnamon oil | |
| CN205980832U (en) | A steam condensate water waste heat retrieval and utilization device for in low -temperature distillation equipment | |
| CN205235415U (en) | Thermal cycle mechanical compression evaporation plant | |
| CN206474058U (en) | A kind of urea for vehicle solution process units | |
| CN106091719B (en) | For the steam condensed water waste heat reclamation set in cryogenic distillation apparatus | |
| CN205241476U (en) | Mud spiral propulsion pyrolysis treatment in vertical cities and towns deals with equipment | |
| CN203408724U (en) | Novel distillation device | |
| CN204058368U (en) | A kind of intermittent type catalytic cracking experimental installation | |
| CN209685562U (en) | A kind of sludge treatment equipment | |
| CN209221530U (en) | A kind of reactive distillation column being easy to material reaction | |
| CN206721122U (en) | A kind of visual crude dehydrating plant | |
| CN207775182U (en) | A kind of orange oil distillation processing concentrator | |
| CN106433732A (en) | Drying or thermal-cracking method for multistage treatment of material | |
| CN106479668A (en) | Device for extracting star anise oil by negative pressure circulating water | |
| CN208599191U (en) | A kind of semicontinuous automation feed liquid vaporising device |
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: 20170315 Termination date: 20180826 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |