CN204310985U - Glycerol production equipment - Google Patents
Glycerol production equipment Download PDFInfo
- Publication number
- CN204310985U CN204310985U CN201420667430.4U CN201420667430U CN204310985U CN 204310985 U CN204310985 U CN 204310985U CN 201420667430 U CN201420667430 U CN 201420667430U CN 204310985 U CN204310985 U CN 204310985U
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- CN
- China
- Prior art keywords
- susceptor
- condenser
- transferpump
- distillation tower
- finished pot
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- Withdrawn - After Issue
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses glycerol production equipment, it comprises multiple dewatering pan, preheater, distillation tower, multiple susceptor, multiple condenser and multiple finished pot, be connected with transferpump bottom dewatering pan, transferpump is connected with preheater by pipeline, be connected with distillation tower top bottom preheater, the first susceptor is connected bottom distillation tower, distillation tower top connects the first condenser, first condenser is connected with the second condenser, second susceptor and the 3rd susceptor are set bottom the first condenser, second susceptor is connected with the 3rd susceptor, 4th susceptor is set bottom the second condenser, second condenser, 3rd condenser is connected transferpump with the bottom of the 4th susceptor, this transferpump connecting tube is to finished pot.Adopt whole plant, glycerol production can be carried out continuously, atmospheric pollution and waste residue, wastewater problem can not be produced; Adopt heat-conducting oil heating running cost low, only need suitably to supplement the thermal oil consumed.
Description
Technical field
The utility model relates to a kind of glycerol production equipment.
Background technology
Glycerine, this product is Glycerin, containing C
3h
8o
3must not 95.0% be less than.Glycerine is one of important industrial chemicals, there is excellent dissolving and wettability, in industry widespread uses such as medicine, food, makeup, chemical industry, in raw glycerine, glycerol content is generally at about 70-80%, the removal of impurities of raw glycerine, decolouring and concentrated, to purify be very difficult, originally Boiler Steam heating can not be carried out continuously, and High Temperature High Pressure brings danger.Therefore, need to provide a kind of new technical scheme to solve the problems referred to above.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of glycerol production equipment.Overcome the heating of original boiler and need successional problem.
For solving the problems of the technologies described above, glycerol production equipment of the present utility model, it comprises multiple dewatering pan, preheater, distillation tower, multiple susceptor, multiple condenser and multiple finished pot, be connected with transferpump bottom described dewatering pan, described transferpump is connected with preheater by pipeline, be connected with distillation tower top bottom described preheater, the first susceptor is connected bottom described distillation tower, described distillation tower top connects the first condenser, described first condenser is connected with the second condenser, second susceptor and the 3rd susceptor are set bottom described first condenser, described second susceptor is connected with the 3rd susceptor, 4th susceptor is set bottom described second condenser, described second susceptor, 3rd susceptor is connected transferpump with the bottom of the 4th susceptor, this transferpump connecting tube is to finished pot.
Multiple dewatering pan is the first dewatering pan and the second dewatering pan, and the first dewatering pan is connected by pipeline with the top of the second dewatering pan.
Multiple finished pot is the first finished pot and the second finished pot, and described first finished pot is connected by pipeline with the top of the second finished pot.
The beneficial effects of the utility model: adopt whole plant, glycerol production can be carried out continuously, atmospheric pollution and waste residue, wastewater problem can not be produced; Adopt heat-conducting oil heating running cost low, only need suitably to supplement the thermal oil consumed.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
1, the first dewatering pan, the 2, second dewatering pan, 3, preheater, 4, distillation tower, the 5, first susceptor, 6, the second susceptor, the 7, the 3rd susceptor, the 8, the 4th susceptor, the 9, first condenser, 10, the second condenser, 11, transferpump, the 12, first finished pot, the 13, second finished pot.
Embodiment
In order to deepen understanding of the present utility model, below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail, and this embodiment, only for explaining the utility model, does not form the restriction to protection domain of the present utility model.
With reference to figure 1, glycerol production equipment of the present utility model, it comprises multiple dewatering pan, preheater 3, distillation tower 4, multiple susceptor, multiple condenser and multiple finished pot, multiple dewatering pan is the first dewatering pan 1 and the second dewatering pan 2, first dewatering pan 1 is connected by pipeline with the top of the second dewatering pan 2, be connected with transferpump 11 bottom dewatering pan, transferpump 11 is connected with preheater 3 by pipeline, be connected with distillation tower 4 top bottom preheater 3, the first susceptor 5 is connected bottom distillation tower 4, distillation tower 4 top connects the first condenser 9, first condenser 9 is connected with the second condenser 10, second susceptor 6 and the 3rd susceptor 7 are set bottom first condenser 9, second susceptor 6 is connected with the 3rd susceptor 7, 4th susceptor 8 is set bottom second condenser 10, second susceptor 6, 3rd susceptor 7 is connected transferpump 11 with the bottom of the 4th susceptor 8, this transferpump 11 connecting tube to the first finished pot 12 and second finished pot 13, first finished pot 12 is connected by pipeline with the top of the second finished pot 13.
Repeatedly adopt heat transfer oil electric heating to heat to dewatering pan, convenient and swift, as long as thermal oil keeps circulation in pipeline, off-set facility storage tank has enough feed supplements (thermal oil) and emptying.Crude product glycerine after dehydration is sent into preheater and carries out pre-heating temperature elevation, glycerine by preheater preheats is entered fractionation in distillation tower again, carry out underpressure distillation, overhead product cools in rearmounted glycerine susceptor through condenser, is entered in finished pot in time by the overhead product in the susceptor of full material by transferpump after twice filtration.Adopt whole plant, glycerol production can be carried out continuously, atmospheric pollution and waste residue, wastewater problem can not be produced; Adopt heat-conducting oil heating running cost low, only need suitably to supplement the thermal oil consumed.
Claims (3)
1. glycerol production equipment, it is characterized in that: it comprises multiple dewatering pan, preheater, distillation tower, multiple susceptor, multiple condenser and multiple finished pot, be connected with transferpump bottom described dewatering pan, described transferpump is connected with preheater by pipeline, be connected with distillation tower top bottom described preheater, the first susceptor is connected bottom described distillation tower, described distillation tower top connects the first condenser, described first condenser is connected with the second condenser, second susceptor and the 3rd susceptor are set bottom described first condenser, described second susceptor is connected with the 3rd susceptor, 4th susceptor is set bottom described second condenser, described second susceptor, 3rd susceptor is connected transferpump with the bottom of the 4th susceptor, this transferpump connecting tube is to finished pot.
2. glycerol production equipment according to claim 1, is characterized in that: multiple dewatering pan is the first dewatering pan and the second dewatering pan, and the first dewatering pan is connected by pipeline with the top of the second dewatering pan.
3. glycerol production equipment according to claim 1, is characterized in that: multiple finished pot is the first finished pot and the second finished pot, and described first finished pot is connected by pipeline with the top of the second finished pot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420667430.4U CN204310985U (en) | 2014-11-11 | 2014-11-11 | Glycerol production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420667430.4U CN204310985U (en) | 2014-11-11 | 2014-11-11 | Glycerol production equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204310985U true CN204310985U (en) | 2015-05-06 |
Family
ID=53133312
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420667430.4U Withdrawn - After Issue CN204310985U (en) | 2014-11-11 | 2014-11-11 | Glycerol production equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204310985U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104447201A (en) * | 2014-11-11 | 2015-03-25 | 上海中华药业南通有限公司 | Glycerol production device and glycerol production process |
-
2014
- 2014-11-11 CN CN201420667430.4U patent/CN204310985U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104447201A (en) * | 2014-11-11 | 2015-03-25 | 上海中华药业南通有限公司 | Glycerol production device and glycerol production process |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150506 Effective date of abandoning: 20170510 |
|
| AV01 | Patent right actively abandoned |