CN107790082A - A kind of glycerine handles reactor - Google Patents
A kind of glycerine handles reactor Download PDFInfo
- Publication number
- CN107790082A CN107790082A CN201610800293.0A CN201610800293A CN107790082A CN 107790082 A CN107790082 A CN 107790082A CN 201610800293 A CN201610800293 A CN 201610800293A CN 107790082 A CN107790082 A CN 107790082A
- Authority
- CN
- China
- Prior art keywords
- glycerine
- main body
- separator box
- inner chamber
- standing groove
- 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.)
- Pending
Links
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 title claims abstract description 104
- 235000011187 glycerol Nutrition 0.000 title claims abstract description 52
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 34
- 238000009833 condensation Methods 0.000 claims abstract description 12
- 230000005494 condensation Effects 0.000 claims abstract description 12
- 239000012530 fluid Substances 0.000 claims description 7
- 239000003610 charcoal Substances 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 description 5
- 238000001914 filtration Methods 0.000 description 3
- 239000000049 pigment Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
- C07C29/76—Separation; Purification; Use of additives, e.g. for stabilisation by physical treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00054—Controlling or regulating the heat exchange system
- B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
- B01J2219/00058—Temperature measurement
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
- B01J2219/00081—Tubes
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
Abstract
The invention discloses a kind of glycerine to handle reactor,Including main body,The intracavity sidewall of the main body is movably installed with activated carbon standing groove close to the lower end of charging aperture,Another side wall in inner chamber of the main body is installed with temperature detector,Bottom is installed with heater strip in the inner chamber of the main body,The outer wall side of the main body is installed with controller,The outer wall opposite side of the main body is provided with drain hole,The end of the escape pipe is installed with condensation chamber,The lower end of the condensation chamber is fixedly connected with separator box by pipeline,The side upper end of the separator box is provided with glycerine delivery hose,The end of the glycerine delivery hose is installed with hydraulic pump,The inner chamber lower end of the separator box is provided with glycerine screen pack,Glycerine processing reactor can more efficiently handle crude glycerine,And high treating effect,Sufficient purified treatment crude glycerine can be compared,It can separate and handle the glycerine of volatilization,Improve the organic efficiency of glycerine.
Description
Technical field
The present invention relates to technical field of food additives, specially a kind of glycerine processing reactor.
Background technology
Crude glycerine, which can isolate some when being pre-processed and float on glycerine upper strata, pigment, and can contain in crude glycerine
The impurity such as a small amount of water, to ensure the smooth production of process below, it is necessary to carry out adsorption filtration to pigment and carried out to glycerine
Purified treatment.But the equipment operation inconvenience for pigment adsorption filtration in the prior art, the equipment replacement of absorption is inconvenient, and
It is huger for the equipment of the purified treatment of glycerine, complicated, operation inconvenience.
The content of the invention
It is an object of the invention to provide a kind of glycerine to handle reactor, is asked with solve to propose in above-mentioned background technology
Topic.
To achieve the above object, the present invention provides following technical scheme：A kind of glycerine handles reactor, including main body, institute
The lower end for stating main body is fixedly connected with the first supporting leg, and motor, the motor are provided with the middle part of the upper surface of the main body
Both sides be respectively arranged with charging aperture and escape pipe, the intracavity sidewall of the main body is movably installed with work close to the lower end of charging aperture
Property charcoal standing groove, another side wall in inner chamber of the main body are installed with temperature detector, and the output shaft end of the motor is consolidated
Surely rotary shaft is connected with, the middle part and lower end of the rotary shaft are installed with puddler, and bottom is consolidated in the inner chamber of the main body
Dingan County is equipped with heater strip, and the outer wall side of the main body is installed with controller, and the outer wall opposite side of the main body is provided with
Drain hole, and the bottom of main body is provided with the first leakage fluid dram, the end of the escape pipe is installed with condensation chamber, the condensation
The lower end of room is fixedly connected with separator box by pipeline, and the side upper end of the separator box is provided with glycerine delivery hose, described
Glycerine delivery hose can be installed with hydraulic pump in separator box internal regulation height, the end of the glycerine delivery hose,
The lower end both sides of the separator box are connected with the second supporting leg, and the second leakage fluid dram, institute are provided among the lower end of the separator box
The inner chamber lower end for stating separator box is provided with glycerine screen pack, and the temperature detector and heater strip are electrically connected with controller.
Preferably, handle is installed with the outside of the activated carbon standing groove, and the lower end of activated carbon standing groove is set
There is supporting plate, the supporting plate is fixedly connected with main body.
Preferably, the upper end of the activated carbon standing groove is set fluted.
Preferably, the lower end of the separator box is arranged to coniform.
Preferably, the port part being connected with main body of the escape pipe is provided with trapezoid-shaped openings.
Preferably, the lower end of the charging aperture is provided with extension block.
Compared with prior art, the beneficial effects of the invention are as follows：Glycerine processing reactor can be handled more efficiently
Crude glycerine, and high treating effect, activated carbon can carry out preliminary treatment to crude glycerine, and activated carbon standing groove passes through bolt
Connection, can be changed, and fixed than stronger, and heater strip heats to device, while has agitating device, can compare and fill
The purified treatment crude glycerine divided, and escape pipe is provided with condensation chamber and separator box, further can separate and handle volatilization
Glycerine, improve the organic efficiency of glycerine.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention；
Fig. 2 is activated carbon standing groove front view of the present invention.
In figure：1 main body, 2 temperature detectors, 3 escape pipes, 4 motor, 5 charging apertures, 6 extension blocks, 7 activated carbon standing grooves,
71 handles, 72 supporting plates, 8 controllers, 9 rotary shafts, 10,11 first supporting legs, 12 second supporting legs, 13 second leakage fluid drams, 14
It is separator box, 15 first leakage fluid drams, 16 pipelines, 17 puddlers, 18 condensation chambers, 19,20 glycerine delivery hoses, 21 drain holes, 22 sweet
Oily screen pack.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, rather than whole embodiments.It is based on
Embodiment in the present invention, those of ordinary skill in the art are obtained every other under the premise of creative work is not made
Embodiment, belong to the scope of protection of the invention.
Fig. 1-2 is referred to, the present invention provides a kind of technical scheme：A kind of glycerine handles reactor, including main body 1, described
The lower end of main body 1 is fixedly connected with the first supporting leg 11, and motor 4 is provided with the middle part of the upper surface of the main body 1, described electronic
The both sides of machine 4 are respectively arranged with charging aperture 5 and escape pipe 3, and the port part being connected with main body 1 of the escape pipe 3 is provided with ladder
Shape opening, can preferably collect steam, and the lower end of the charging aperture 5 is provided with extension block 6, activated carbon standing groove 7 is played
More preferable supporting role, the intracavity sidewall of the main body 1 are movably installed with activated carbon standing groove 7, institute close to the lower end of charging aperture 5
The outside for stating activated carbon standing groove 7 is installed with handle 71, and the lower end of activated carbon standing groove 7 is provided with supporting plate 72, institute
State supporting plate 72 to be fixedly connected with main body 1, the upper end setting of the activated carbon standing groove 7 is fluted, can make the liquid of entrance
Preferably filtering, another side wall in inner chamber of the main body 1 are installed with temperature detector 2, the output shaft end of the motor 4
It is fixedly connected with rotary shaft 9, the middle part and lower end of the rotary shaft 9 are installed with puddler 17, in the inner chamber of the main body 1
Bottom is installed with heater strip 10, and the outer wall side of the main body 1 is installed with controller 8, and the outer wall of the main body 1 is another
Side is provided with drain hole 21, and the outer wall opposite side of the main body 1 is provided with drain hole 21, and the bottom of main body 1 is provided with
One leakage fluid dram 15, the end of the escape pipe 3 are installed with condensation chamber 18, and the lower end of the condensation chamber 18 is solid by pipeline 16
Surely separator box 14 is connected with,：The lower end of the separator box 14 is arranged to coniform, and the side upper end of the separator box 14 is provided with
Glycerine delivery hose 20, the glycerine delivery hose 20 can be in the internal regulation of separator box 14 height, the glycerine delivery hoses
20 end is installed with hydraulic pump 19, and the lower end both sides of the separator box 14 are connected with the second supporting leg 12, the separation
The second leakage fluid dram 13 is provided among the lower end of case 14, the inner chamber lower end of the separator box 14 is provided with glycerine screen pack 22, institute
State temperature detector 2 and heater strip 10 is electrically connected with controller 8.
Operation principle：Crude glycerine is entered by charging aperture 5 in the inner chamber of main body 1, and activated carbon can carry out preliminary to liquid
Purified treatment, then motor 4 can drive the rotation of rotary shaft 9, then the puddler 17 in rotary shaft 9 can be in main body
Crude glycerine be stirred, while heater strip 10 can heat to the liquid in main body 1, and temperature detector 2 can detect
Temperature in the inner chamber of main body 1, then sending instruction to controller 8 at any time, controller 8 controls the break-make of heater strip 10, so as to
The temperature inside main body 1 is controlled, the heated boil-off gas of liquid enters condensation chamber 8 by escape pipe 3, by condensation chamber 8
Steam become liquid separator box 14 entered by pipeline 16, the glycerine screen pack 22 in separator box 14 can filter out glycerine and
Water, glycerine delivery hose 20 can pump out glycerine in the presence of hydraulic pump 19, and drain hole 21 can purify to being put into main body 1
Material, facilitates the purification of crude glycerine.
Although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
A variety of changes, modification can be carried out to these embodiments, replace without departing from the principles and spirit of the present invention by understanding
And modification, the scope of the present invention is defined by the appended.
Claims (6)
1. a kind of glycerine handles reactor, including main body (1), it is characterised in that：The lower end of the main body (1) is fixedly connected with
One supporting leg (11), the upper surface middle part of the main body (1) are provided with motor (4), and the both sides of the motor (4) are set respectively
Charging aperture (5) and escape pipe (3) are equipped with, the intracavity sidewall of the main body (1) is movably installed with work close to the lower end of charging aperture (5)
Property charcoal standing groove (7), another side wall in inner chamber of the main body (1) are installed with temperature detector (2), the motor (4)
Output shaft end be fixedly connected with rotary shaft (9), the middle part and lower end of the rotary shaft (9) are installed with puddler (17),
Bottom is installed with heater strip (10) in the inner chamber of the main body (1), and the outer wall side of the main body (1) is installed with control
Device (8) processed, the outer wall opposite side of the main body (1) is provided with drain hole (21), and the bottom of main body (1) is provided with the first discharge opeing
Mouth (15), the end of the escape pipe (3) are installed with condensation chamber (18), and the lower end of the condensation chamber (18) passes through pipeline
(16) separator box (14) is fixedly connected with, the side upper end of the separator box (14) is provided with glycerine delivery hose (20), described
Glycerine delivery hose (20) can fix peace in separator box (14) internal regulation height, the end of the glycerine delivery hose (20)
Equipped with hydraulic pump (19), the lower end both sides of the separator box (14) are connected with the second supporting leg (12), the separator box (14)
The second leakage fluid dram (13) is provided among lower end, the inner chamber lower end of the separator box (14) is provided with glycerine screen pack (22), institute
Temperature detector (2) and heater strip (10) is stated to be electrically connected with controller (8).
A kind of 2. glycerine processing reactor according to claim 1, it is characterised in that：The activated carbon standing groove (7)
Outside is installed with handle (71), and the lower end of activated carbon standing groove (7) is provided with supporting plate (72), the supporting plate (72)
It is fixedly connected with main body (1).
A kind of 3. glycerine processing reactor according to claim 1, it is characterised in that：The activated carbon standing groove (7)
Upper end sets fluted.
A kind of 4. glycerine processing reactor according to claim 1, it is characterised in that：The lower end of the separator box (14) is set
It is set to coniform.
A kind of 5. glycerine processing reactor according to claim 1, it is characterised in that：The escape pipe (3) and main body
(1) port part of connection is provided with trapezoid-shaped openings.
A kind of 6. glycerine processing reactor according to claim 1, it is characterised in that：The lower end of the charging aperture (5) is set
It is equipped with extension block (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610800293.0A CN107790082A (en) | 2016-08-31 | 2016-08-31 | A kind of glycerine handles reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610800293.0A CN107790082A (en) | 2016-08-31 | 2016-08-31 | A kind of glycerine handles reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107790082A true CN107790082A (en) | 2018-03-13 |
Family
ID=61530586
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610800293.0A Pending CN107790082A (en) | 2016-08-31 | 2016-08-31 | A kind of glycerine handles reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107790082A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108469369A (en) * | 2018-05-11 | 2018-08-31 | 广东产品质量监督检验研究院（国家质量技术监督局广州电气安全检验所、广东省试验认证研究院、华安实验室） | Solid Phase Extraction-nitrogen blows concentration integrated device |
-
2016
- 2016-08-31 CN CN201610800293.0A patent/CN107790082A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108469369A (en) * | 2018-05-11 | 2018-08-31 | 广东产品质量监督检验研究院（国家质量技术监督局广州电气安全检验所、广东省试验认证研究院、华安实验室） | Solid Phase Extraction-nitrogen blows concentration integrated device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180313 |
|
| WD01 | Invention patent application deemed withdrawn after publication |