CN204485872U - A kind of distillation reactor - Google Patents
A kind of distillation reactor Download PDFInfo
- Publication number
- CN204485872U CN204485872U CN201420861743.3U CN201420861743U CN204485872U CN 204485872 U CN204485872 U CN 204485872U CN 201420861743 U CN201420861743 U CN 201420861743U CN 204485872 U CN204485872 U CN 204485872U
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- Prior art keywords
- annular component
- evaporation member
- component
- annular
- channel
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of distillation reactor, comprise housing, the top of described housing is provided with outlet, in described housing, there is reaction chamber, be provided with in described reaction chamber and be provided with several spaced upper evaporation member and lower evaporation member from top to bottom successively, the cross section flue of described upper evaporation member, the bigger diameter end of evaporation member is arranged upward; The inwall of described evaporation member is provided with the first annular component and the second annular component from outside to inside successively, described first annular component has the first ring-type member aperture, second annular component has the second annular component breach, and the center of evaporation member is provided with small opening.
Description
Technical field
The utility model relates to a kind of reactor, particularly a kind of distillation reactor.
Background technology
At present, distillation reactor is the common equipment in the production process of chemical industry, and operation principle is the difference according to cut boiling point, will need the feed vaporization of distillation, then is collected by condensation, can complete distillation.
In distillation procedure, when some organic matters are heated near its normal boiling point, can be too high and be oxidized, decompose or the reaction such as polymerization due to temperature, it is made to distill at ambient pressure, by decompression distillation still is connected on a set of depressurized system, before distillation starts, first make whole system pressure be reduced to only have ten part to tens/mono-of normal pressure, so this type organic just can distill at the temperature much lower compared with its normal boiling point.
Existing decompression distillation still is due to the restriction of its structure, and distillation efficiency is low, wastes energy, and needs the material distilled, distillation insufficient, cause the waste of raw material in still-process Raw.
summary of the invention [0005]problem to be solved in the utility model is to provide for the deficiencies in the prior art, provides a kind of distillation reactor, and this distillation reactor can distill liquid material easily, and distillation fully.
For solving the problem, the technical scheme that the utility model adopts is:
A kind of distillation reactor, comprise housing, the top of described housing is provided with outlet, has reaction chamber in described housing,
Be provided with in described reaction chamber and be provided with several spaced upper evaporation member and lower evaporation member from top to bottom successively,
The cross section flue of described upper evaporation member, the bigger diameter end of evaporation member is arranged upward; The inwall of described evaporation member is provided with the first annular component and the second annular component from outside to inside successively, described first annular component has the first ring-type member aperture, second annular component has the second annular component breach, and the center of evaporation member is provided with small opening;
The cross section flue of described lower evaporation member, the bigger diameter end of lower evaporation member is downward, the outer wall of described lower evaporation member is provided with from outside to inside successively the 3rd annular component, the 4th annular component and the 5th annular component, the center of circle of described lower evaporation member has projection; 3rd annular component has the 3rd annular component breach, the 4th annular component has the 4th ring-type member aperture, the 5th annular component has the 6th annular component breach.
Below the further improvement to technique scheme:
Form first passage between evaporation member edge and the first annular component, form second channel between the first annular component and the second annular component, between the second annular component and small opening, form third channel.
Described 5th forms four-way between annular component and projection, forms Five-channel between the 4th annular component and the 5th annular component, forms Hexamermis spp between the 4th annular component and the 3rd annular component.
Be provided with hydrojet component in reaction chamber, described hydrojet component comprises shower tray, and described shower tray is evenly equipped with several nozzles around the shower tray center of circle.
During use, heating tube heats, and liquid material is sprayed onto evaporation member from hydrojet component, and liquid material flows downward due to the endways evaporation member inwall of effect of gravity, enters into first passage, second channel and third channel and evaporates, described first annular component has the first ring-type member aperture, second annular component has the second annular component breach, second channel can be entered into easily in the liquid material of first passage and proceed evaporation, residue liquid material after evaporation enters lower evaporation member by small opening and evaporates, due to lower evaporation member bigger diameter end down, liquid enters into four-way due to the effect of gravity, Five-channel and Hexamermis spp, continue evaporation, last feed liquid flow into waste collection chamber, the utility model is used to distill, distilling effect is good, the utilization rate of liquid material is high, decrease the waste of resource, improve liquid material utilization rate.
Below in conjunction with accompanying drawing, the invention will be further described.
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation of a kind of distillation reactor of the present utility model;
Accompanying drawing 2 is upper evaporation member structural representation in embodiment;
Accompanying drawing 3 is the sectional view of accompanying drawing 2;
Accompanying drawing 4 is the structural representation of lower evaporation member in embodiment;
Accompanying drawing 5 is the sectional view of accompanying drawing 4.
In figure:
1-housing; 2-exports; 3-heating tube; 4-feed line; 5-hydrojet component; 51-shower tray; 6-nozzle; The upper evaporation member of 7-; Evaporation member under 8-; 9-waste collection chamber; 10-motor; 11-stirring vane; 12-circulating pump; 13-feed pipe; 14-reaction chamber; 71-first annular component; 72-first ring-type member aperture; 73-second annular component; 74-second annular component breach; 75-small opening; 77-first passage; 78-second channel; 79-third channel; 81-the 3rd annular component; 82-the 3rd annular component breach; 83-the 4th annular component; 84-the 4th ring-type member aperture; 85-the 5th annular component; 86-the 6th annular component breach; 87-is protruding; 88-four-way; 89-Five-channel; 90-Hexamermis spp.
Detailed description of the invention
Embodiment, as shown in accompanying drawing 1, accompanying drawing 2, accompanying drawing 3 and accompanying drawing 4, a kind of distillation reactor, comprises housing 1, and the top of described housing 1 is provided with outlet 2, has reaction chamber 14 and waste collection chamber 9 in described housing 1.
Be provided with in described reaction chamber 8 and be provided with several evaporation member successively from top to bottom, the top of described each evaporation member is provided with hydrojet component 5.
Described evaporation member comprises evaporation member 7 and lower evaporation member 8, and upper evaporation member 7 and lower evaporation member 8 interval are arranged, the cross section flue of described upper evaporation member 7, and the bigger diameter end of evaporation member 7 is arranged upward; The inwall of described evaporation member 7 is provided with from outside to inside successively the first annular component 71 and the second annular component 73, described first annular component 71 has the first ring-type member aperture 72, second annular component 73 has the second annular component breach 74, and the center of evaporation member 7 is provided with small opening 75.
Form first passage 77 between evaporation member 7 edge and the first annular component 71, formed between second channel 78, second annular component 73 and small opening 75 between the first annular component 71 and the second annular component 73 and form third channel 79.
Described first annular component 71 and the second annular component 73 are in annular.
The cross section flue of described lower evaporation member 8, the bigger diameter end of lower evaporation member 8 is downward, the outer wall of described lower evaporation member 8 is provided with from outside to inside successively the 3rd annular component 81, the 4th annular component 83 and the 5th annular component 85, the center of circle of described lower evaporation member 8 has protruding 87; 3rd annular component 81 has the 3rd annular component breach the 82, four annular component 83 has on the 4th ring-type member aperture the 84, five annular component 85 and there is the 6th annular component breach 86.
Form four-way 88 between described 5th annular component 85 and protruding 87, form Five-channel 89 between the 4th annular component 83 and the 5th annular component 85, between the 4th annular component 83 and the 3rd annular component 81, form Hexamermis spp 90.
Described hydrojet component 5 comprises shower tray 51, and described shower tray 51 is evenly equipped with several nozzles 6 around shower tray 51 center of circle.
Nozzle 6 extend in first passage 77, second channel 78 and third channel 79.
Nozzle 6 extend in four-way 88, the 5th circular passage 89 and Hexamermis spp 90.
Reaction chamber 8 internal fixtion is provided with feed line 4, and described feed line 4 is communicated with hydrojet component 5, and described feed line 4 is communicated with raw material inlet pipe 13.
Waste collection chamber 9 is arranged on the bottom of housing 1.
Be provided with agitating device in described collection chamber 9, described agitating device comprises stirring vane 11, and stirring vane 11 and the motor 10 be arranged on bottom housing 1 are in transmission connection.
Described collection chamber 9 is communicated with circulating pump 12, and circulating pump 12 is communicated with raw material inlet pipe 13.
Heating tube 3 is provided with in described housing 1.
During use, heating tube 3 heats, and liquid material is sprayed onto evaporation member 7 from hydrojet component 5, and liquid material flows downward due to effect endways evaporation member 7 inwall of gravity, enters into first passage 77, second channel 78 and third channel 79 and evaporates, described first annular component 71 has the first ring-type member aperture 72, second annular component 73 has the second annular component breach 74, second channel 78 can be entered into easily in the liquid material of first passage 77 and proceed evaporation, residue liquid material after evaporation enters lower evaporation member 8 by small opening 75 and evaporates, due to lower evaporation member 8 bigger diameter end down, liquid enters into four-way 88 due to the effect of gravity, Five-channel 89 and Hexamermis spp 90, continue evaporation, last feed liquid flow into waste collection chamber 9, the utility model is used to distill, distilling effect is good, the utilization rate of liquid material is high, decrease the waste of resource, improve liquid material utilization rate.
Claims (4)
1. a distillation reactor, comprises housing (1), and the top of described housing (1) is provided with outlet (2), has reaction chamber (14) in described housing (1),
Be provided with in described reaction chamber (14) and be provided with several spaced upper evaporation member (7) and lower evaporation member (8) from top to bottom successively,
The cross section flue of described upper evaporation member (7), the bigger diameter end of evaporation member (7) is arranged upward; The inwall of described evaporation member (7) is provided with from outside to inside successively the first annular component (71) and the second annular component (73), described first annular component (71) has the first ring-type member aperture (72), second annular component (73) has the second annular component breach (74), and the center of evaporation member (7) is provided with small opening (75);
The cross section flue of described lower evaporation member (8), the bigger diameter end of lower evaporation member (8) is downward, the outer wall of described lower evaporation member (8) is provided with from outside to inside successively the 3rd annular component (81), the 4th annular component (83) and the 5th annular component (85), the center of circle of described lower evaporation member (8) has projection (87); 3rd annular component (81) has the 3rd annular component breach (82), the 4th annular component (83) has the 4th ring-type member aperture (84), the 5th annular component (85) has the 6th annular component breach (86).
2. a kind of distillation reactor as claimed in claim 1, it is characterized in that: between evaporation member (7) edge and the first annular component (71), form first passage (77), form second channel (78) between the first annular component (71) and the second annular component (73), between the second annular component (73) and small opening (75), form third channel (79).
3. a kind of distillation reactor as claimed in claim 2, it is characterized in that: between described 5th annular component (85) and protruding (87), form four-way (88), form Five-channel (89) between 4th annular component (83) and the 5th annular component (85), between the 4th annular component (83) and the 3rd annular component (81), form Hexamermis spp (90).
4. a kind of distillation reactor as claimed in claim 3, it is characterized in that: in reaction chamber (14), be provided with hydrojet component (5), described hydrojet component (5) comprises shower tray (51), and described shower tray (51) is evenly equipped with several nozzles (6) around shower tray (51) center of circle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420861743.3U CN204485872U (en) | 2014-12-31 | 2014-12-31 | A kind of distillation reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420861743.3U CN204485872U (en) | 2014-12-31 | 2014-12-31 | A kind of distillation reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204485872U true CN204485872U (en) | 2015-07-22 |
Family
ID=53565168
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420861743.3U Expired - Fee Related CN204485872U (en) | 2014-12-31 | 2014-12-31 | A kind of distillation reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204485872U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109011673A (en) * | 2018-08-28 | 2018-12-18 | 江苏博勤氟塑科技有限公司 | A kind of distillation condensing unit for strong acid and strong base |
-
2014
- 2014-12-31 CN CN201420861743.3U patent/CN204485872U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109011673A (en) * | 2018-08-28 | 2018-12-18 | 江苏博勤氟塑科技有限公司 | A kind of distillation condensing unit for strong acid and strong base |
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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: 20150722 Termination date: 20151231 |
|
| EXPY | Termination of patent right or utility model |