CN102179058A - Distillation reactor - Google Patents
Distillation reactor Download PDFInfo
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- CN102179058A CN102179058A CN201110041937XA CN201110041937A CN102179058A CN 102179058 A CN102179058 A CN 102179058A CN 201110041937X A CN201110041937X A CN 201110041937XA CN 201110041937 A CN201110041937 A CN 201110041937A CN 102179058 A CN102179058 A CN 102179058A
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Abstract
The invention discloses a distillation reactor, which comprises an accommodating cavity. A heating rod is inserted into the accommodating cavity; the accommodating cavity is provided with an essence inlet, a steam outlet and a slag discharge hole; an outer layer with a cavity is coated at the outer periphery of the accommodating cavity; the outer layer is provided with a steam circulating inlet and a steam circulating outlet; the outer layer positioned at the bottom of the accommodating cavity is provided with a liquid outlet; and the steam circulating inlet is communicated with a steam outlet. The outer periphery of the accommodating cavity is coated with the outer layer with the cavity, steam generated by heating the reactor enters the cavity of an insulating layer through the steam circulating inlet, and is circulated in the cavity and discharged through the steam outlet, the energy loss of the accommodating cavity of the reactor is reduced, the heat insulation function is realized and the heating energy is saved.
Description
Technical field
The invention belongs to the heating distillation equipment, specifically relate to a kind of distillation reactor for preparing the living beings distillate.
Background technology
Biomass energy is the solar energy that is stored in by the photosynthesis of plant and solar energy in the plant.According to estimates, the annual energy of storing of plant is equivalent to 10 times that world's main fuel consumes, and is less than 1% of its total amount as the utilization of the energy.Characteristics such as biomass material is because of having the volatility height, and carbon is active high, and N, S content are low, and ash content is low are a kind of fuel of high-quality.By the biomass energy switch technology, can utilize this reproducible clean biomass energy efficiently, be converted into ecological oil, substitute fuel such as coal, oil and natural gas.
Ecological oil can also further be purified except can be used as fuel, makes pyrolkigneous liquid, with the further deep processing of pyrolkigneous liquid, can also make vegetalitas hand cleanser, footbath liquor etc. as again.
The reactor of the preparation hand cleanser of prior art, it has cavity volume and several import and export, and is simple in structure, can not the recycling requirement of the clean energy of the Qing Dynasty, energy consumption is quite big, must improve the structure of reactor.
Summary of the invention
In order to solve the problem that prior art exists, the distillate that the invention provides after a kind of distillation can be as heat medium with recycling reactor.
In order to realize above purpose, technical scheme of the present invention is as follows: comprise cavity volume, be plugged with heating rod in the cavity volume, cavity volume has Essence inlet, steam (vapor) outlet, slag-drip opening, the exterior circumferential of described cavity volume is coated with the skin that one deck has cavity, described skin is provided with vapor recycle inlet and vapor recycle outlet, and the skin place that is positioned at the cavity volume bottom is provided with leakage fluid dram, and described vapor recycle inlet is communicated with steam (vapor) outlet.
Further, described cavity volume is provided with venting.
Described cavity volume is provided with temperature inductor.
Described cavity is provided with liquid level alarm, aligns with the bottom of heating rod in the bottom of liquid level alarm.
The sidewall of described cavity is provided with liquid level gauge, and the mouth of detection up and down of described liquid level gauge is obliquely installed.
Described steam (vapor) outlet is arranged at the top of cavity volume.
The present invention is owing to have the skin of cavity at the periphery of cavity volume parcel one deck, the steam that produces in the reactor heating enters the cavity of heat-insulation layer from the vapor recycle inlet, come out from steam (vapor) outlet in the circulation back in cavity, reduced the loss of the cavity volume energy of reactor, play insulation effect, save heat energy.
Description of drawings
Fig. 1 is the structural representation of distillation reactor of the present invention.
Below, in conjunction with the embodiments and accompanying drawing, the present invention is described in further detail.
The specific embodiment
As shown in Figure 1, the distillation reactor main body is a cylindrical shape cavity volume 3, the top of cavity volume 3 is provided with Essence inlet 6, venting 5, steam (vapor) outlet 7, cavity volume 3 tops also are plugged with temperature inductor 4 and liquid level alarm 8, temperature inductor 4 is positioned at the top of cavity volume, and liquid level alarm 8 extends to heating rod 1 level place.Periphery parcel one deck skin 2 of cavity volume 3, this skin has cavity.Outer 2 are provided with vapor recycle inlet 9 and vapor recycle outlet 15.The vapor recycle inlet 9 of the steam (vapor) outlet 7 of cavity volume 3 and outer 2 cavity is communicated with by pipeline.The bottom of cavity volume 3 is plugged with heating rod 1, and the Essence in the cavity volume is heated, and makes generation steam.The sidewall of cavity volume 3 is equipped with liquid level gauge 11, and detection mouth 10 is obliquely installed with the following mouth 12 that detects on it, promptly is that the center line and the sidewall of detection mouth is non-perpendicular.The bottom centre position of cavity volume 3 offers slag-drip opening 14, and the bottom of outer 2 cavity also offers leakage fluid dram 14.
The operation principle of distillation reactor is as follows: a certain amount of Essence in the cavity volume, by heating rod be heated to 80 the degree more than begin to produce steam, after steam enters the vapor recycle inlet from steam (vapor) outlet, steam circulates in cavity, export from the vapor recycle outlet at last, and the residue behind the distillation reaction is mainly the low molecular weight cellulose fragment.Distillation leftover falls to the bottom of cavity volume, can be discharged by slag-drip opening.When the liquid level in the cavity volume was lower than heating rod, liquid level alarm was reported to the police.Heat exchange takes place by contacting with cavity volume in the cyclic process of steam in cavity, has both realized the insulation effect to cavity volume, has reduced the temperature of steam again, has reduced the energy consumption of reactor, possesses environment-friendly function.
Claims (6)
1. distillation reactor, comprise cavity volume, be plugged with heating rod in the cavity volume, cavity volume has Essence inlet, steam (vapor) outlet, slag-drip opening, it is characterized in that: the exterior circumferential of described cavity volume is coated with the skin that one deck has cavity, described skin is provided with vapor recycle inlet and vapor recycle outlet, and the skin place that is positioned at the cavity volume bottom is provided with leakage fluid dram, and described vapor recycle inlet is communicated with steam (vapor) outlet.
2. distillation reactor according to claim 1 is characterized in that described cavity volume is provided with venting.
3. distillation reactor according to claim 1 is characterized in that described cavity volume is provided with temperature inductor.
4. distillation reactor according to claim 1 is characterized in that described cavity is provided with liquid level alarm, aligns with the bottom of heating rod in the bottom of liquid level alarm.
5. distillation reactor according to claim 1 is characterized in that the sidewall of described cavity is provided with liquid level gauge, and the mouth of detection up and down of described liquid level gauge is obliquely installed.
6. distillation reactor according to claim 1 is characterized in that described steam (vapor) outlet is arranged at the top of cavity volume.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110041937XA CN102179058A (en) | 2011-02-22 | 2011-02-22 | Distillation reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110041937XA CN102179058A (en) | 2011-02-22 | 2011-02-22 | Distillation reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102179058A true CN102179058A (en) | 2011-09-14 |
Family
ID=44565460
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110041937XA Pending CN102179058A (en) | 2011-02-22 | 2011-02-22 | Distillation reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102179058A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854134A (en) * | 2018-09-18 | 2018-11-23 | 浙江东江能源科技有限公司 | A kind of glycerol separation quick reaction device |
| CN110721639A (en) * | 2018-07-17 | 2020-01-24 | 武汉氢阳能源有限公司 | Reaction device and application thereof |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2102145U (en) * | 1991-09-13 | 1992-04-22 | 何挺佳 | High-efficiency energy-saving distillation equipment |
| CN2260610Y (en) * | 1996-06-07 | 1997-08-27 | 崔习民 | General full-function extracter |
| CN101077459A (en) * | 2006-05-25 | 2007-11-28 | 涂晶 | Regeneration processing device for waste lubricant oil |
-
2011
- 2011-02-22 CN CN201110041937XA patent/CN102179058A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2102145U (en) * | 1991-09-13 | 1992-04-22 | 何挺佳 | High-efficiency energy-saving distillation equipment |
| CN2260610Y (en) * | 1996-06-07 | 1997-08-27 | 崔习民 | General full-function extracter |
| CN101077459A (en) * | 2006-05-25 | 2007-11-28 | 涂晶 | Regeneration processing device for waste lubricant oil |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110721639A (en) * | 2018-07-17 | 2020-01-24 | 武汉氢阳能源有限公司 | Reaction device and application thereof |
| CN108854134A (en) * | 2018-09-18 | 2018-11-23 | 浙江东江能源科技有限公司 | A kind of glycerol separation quick reaction device |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20110914 |