CN107126918A - A kind of high yield biodiesel prepares reactor - Google Patents
A kind of high yield biodiesel prepares reactor Download PDFInfo
- Publication number
- CN107126918A CN107126918A CN201710557884.4A CN201710557884A CN107126918A CN 107126918 A CN107126918 A CN 107126918A CN 201710557884 A CN201710557884 A CN 201710557884A CN 107126918 A CN107126918 A CN 107126918A
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- Prior art keywords
- tank body
- plate
- outer tank
- agitating shaft
- high yield
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Classifications
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- 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
- B01J19/1868—Stationary reactors having moving elements inside resulting in a loop-type movement
- B01J19/1881—Stationary reactors having moving elements inside resulting in a loop-type movement externally, i.e. the mixture leaving the vessel and subsequently re-entering it
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
- C11C3/10—Ester interchange
-
- 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
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
Reactor is prepared the invention discloses a kind of high yield biodiesel, including outer tank body and inner tank body, the inner tank body is located at the inner side of outer tank body, space between inner tank body and outer tank body is heating chamber, the inner space of inner tank body is reaction chamber, the middle part of reaction chamber is provided with agitating shaft vertically, the top of outer tank body is provided with the motor being connected with agitating shaft, the middle part of reaction chamber is in being provided with rabbling mechanism on agitating shaft, the upside of rabbling mechanism is provided with water conservancy diversion web plate, provided with multiple support bars being connected with agitating shaft in the pod apertures of water conservancy diversion web plate, the downside agitating shaft lower end of rabbling mechanism is provided with material scraping plate, the downside of material scraping plate is provided with the screen pack being engaged with material scraping plate, the middle part connection of screen pack is provided with circulation pipe, circulation pipe is provided with circulating pump, the other end of circulation pipe is located in the reaction chamber on the upside of water conservancy diversion web plate.Structure of the present invention is novel, and material mixing Quick uniform in reactor, raw material availability is high, and yield is higher.
Description
Technical field
The present invention relates to production of biodiesel technical field, specifically a kind of high yield biodiesel prepares reactor.
Background technology
Biodiesel refers to oil crops such as soybean, rape, cotton, palm etc., Wild oil plant and engineering microalgae etc.
Water plant grease and animal fat, food garbage oil etc. be feedstock oil by ester exchange or thermochemical processes be made can generation
For the reproducibility diesel fuel of petrifaction diesel.Biodiesel is as the highly preferred renewable sources of energy at this stage, increasingly by weight
Depending on, the reason for its is preferred is that biodiesel molecular weight is close with diesel oil, has similar burning and dynamic characteristics to mineral diesel,
And product is more environmentally-friendly, so the petroleum diesel substitute as high-quality.The preparation method of biodiesel mainly has four kinds, including
Direct mixing method, mini-emulsion process, high temperature pyrolytic cracking and ester-interchange method, wherein ester-interchange method are current most studies and industrial
The method of metaplasia production, ester-interchange method is Bu Tong divided into base-catalyzed transesterification method, acid again due to the different and catalyst of glyceride stock
Catalytic transesterification method, biological enzyme ester-interchange method and overcritical ester-interchange method.
During biodiesel is manufactured by Ester exchange technique, reaction unit is core in biodiesel manufacturing process
One of equipment.The quality of reaction unit determines the quality of the efficiency, energy consumption and biodiesel of biodiesel manufacture.Existing life
Thing diesel oil reaction unit has that structure is single, and the reaction time is long, low production efficiency, and the utilization rate of raw material is not high, influences yield.
The content of the invention
Reactor is prepared it is an object of the invention to provide a kind of high yield biodiesel, to solve to carry in above-mentioned background technology
The problem of going out.
To achieve the above object, the present invention provides following technical scheme：
A kind of high yield biodiesel prepares reactor, including outer tank body and inner tank body, and the inner tank body is located at the inner side of outer tank body,
Space between inner tank body and outer tank body is heating chamber, and the inner space of inner tank body is reaction chamber, the top of the outer tank body
Provided with the row connected with reaction chamber in the middle of the feed pipe and catalyst tube that She You do not connected with reaction chamber, the bottom of the outer tank body
The cold and hot matchmaker's outlet pipe connected with heating chamber is additionally provided with the top of expects pipe, the outer tank body, the bottom of outer tank body is additionally provided with and heated
Multiple pillars are additionally provided with cold and hot matchmaker's inlet pipe of chamber connection, the heating chamber, the middle part of the reaction chamber is provided with agitating shaft vertically,
The crown center of outer tank body is provided with the motor being connected with agitating shaft, and agitating shaft is that sealing rotates company with outer tank body and inner tank body
Connect, the middle part of the reaction chamber is in being provided with rabbling mechanism on agitating shaft, rabbling mechanism includes puddler and agitating plate, described to stir
Plate is mixed for semicircular plate, the both sides of agitating shaft are mounted on offering some second through holes on agitating plate, agitating plate, agitating plate
Outside is provided with some puddlers, and puddler is horizontally disposed with, and puddler is in the same plane with agitating plate, the rabbling mechanism
Upside is provided with water conservancy diversion web plate, and water conservancy diversion web plate is the downwardly projecting pyramidal structure in middle part, the outer ring of water conservancy diversion web plate and inner tank body it is interior
Wall is in offer to be provided with multiple be connected with agitating shaft admittedly in pod apertures, pod apertures in the middle part of one 3~5cm gap, water conservancy diversion web plate
Fixed support bar, the downside agitating shaft lower end of the rabbling mechanism be provided with material scraping plate, material scraping plate offer some first lead to
Hole, the downside of material scraping plate is provided with the screen pack being engaged with material scraping plate, and the outer ring of screen pack and the inwall of inner tank body are fixed
Connection, the middle part connection of the screen pack is provided with circulation pipe, and circulation pipe is provided with circulating pump, and the other end of circulation pipe, which is located at, leads
In reaction chamber on the upside of drift net plate.
It is used as further scheme of the invention：The outer tank body and inner tank body be two ends to outer arcuate protrude it is totally-enclosed
Cylindrical tube structure.
It is used as further scheme of the invention：The pillar is albronze cylinder, and inner tank body is fixed in one end of pillar
Outer wall on, the other end of pillar is fixed on the inwall of outer tank body.
It is used as further scheme of the invention：The support bar is circumferentially uniformly provided with three.
It is used as further scheme of the invention：The material scraping plate is the recessed arc in middle part.
It is used as further scheme of the invention：The outlet of the feed pipe, catalyst tube and circulation pipe is positioned at pod apertures
Above outside.
It is used as further scheme of the invention：The first through hole, the second through hole and pod apertures are circular port or just many
Side shape hole.
It is used as further scheme of the invention：Regulating valve is equipped with cold and hot matchmaker's inlet pipe and cold and hot matchmaker's outlet pipe.
Compared with prior art, the beneficial effects of the invention are as follows：The high yield biodiesel prepares reactor, passes through feed pipe
Grease and catalyst can be added with catalyst tube, motor can drive agitating shaft to rotate, grease and catalyst drop into water conservancy diversion web plate
On, can be lower by the directly filter of water conservancy diversion web plate or it throw away or be flowed down from pod apertures from the centrifugation of water conservancy diversion web plate outer ring, beneficial to grease and urge
The contact fusion of agent, being coordinated by the agitating plate and puddler of rabbling mechanism can be beneficial to oil to material stirring, the second through hole
Fat, catalyst refinement separation, have further speeded up the fusion haptoreaction of grease and catalyst, have improved the speed of esterification reaction
And reaction mass, material is beneficial under screen pack filter by the material scraping plate of rotation and the first through hole opened up thereon, screen pack
Defective material on plate can be dropped into circulation pipe, and circulation conveying reaction is carried out by circulating pump, and the raw material of lifting biodiesel is utilized
Rate；Cold and hot matchmaker is passed through into heating chamber by cold and hot matchmaker's inlet pipe, the temperature beneficial to reaction is adapted to, and can be discharged by cold and hot matchmaker's outlet pipe
Cold and hot matchmaker；Stability between outer tank body and inner tank body can both be lifted by pillar, the enrichment of heat is beneficial to again so that reaction
The temperature change of chamber is permanent steady；The apparatus structure is novel, and material mixing Quick uniform in reactor, raw material availability is high, yield compared with
It is high.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
Fig. 2 is the overlooking the structure diagram of flow-guiding screen plate part in the present invention.
Fig. 3 is the structural representation of rabbling mechanism in the present invention.
In figure：1- feed pipes, 2- catalyst tubes, 3- motors, the cold and hot matchmaker's outlet pipes of 4-, 5- circulation pipes, 6- pillars, 7- outer tanks
Body, 8- heating chambers, 9- inner tank bodys, 10- circulating pumps, 11- first through hole, 12- material scraping plates, 13- drainage conduits, the cold and hot matchmaker's inlet pipes of 14-,
15- screen packs, 16- rabbling mechanisms, 17- agitating shafts, 18- water conservancy diversion web plates, 19- reaction chambers, 20- support bars, 21- pod apertures,
22- agitating plates, the through holes of 23- second, 24- puddlers.
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 is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Refer in Fig. 1~3, the embodiment of the present invention, a kind of high yield biodiesel prepares reactor, including the He of outer tank body 7
Inner tank body 9, the outer tank body 7 and inner tank body 9 are the totally-enclosed cylindrical tube structure that two ends are protruded to outer arcuate, inner tank body
9 are located at the inner side of outer tank body 7, and the space between inner tank body 9 and outer tank body 7 is heating chamber 8, and the inner space of inner tank body 9 is anti-
Chamber 19 is answered, the top of the outer tank body 7 is respectively equipped with the feed pipe 1 and catalyst tube 2 that are connected with reaction chamber 19, passes through feed pipe
1 and catalyst tube 2 can be used in the middle of the addition of material and catalyst, the bottom of the outer tank body 7 provided with being connected with reaction chamber 19
Drainage conduit 13, material is discharged by the cocoa of drainage conduit 13, in order that biodiesel is prepared within the scope of the suitable temperature, institute
The top for stating outer tank body 7 is additionally provided with the cold and hot matchmaker's outlet pipe 4 connected with heating chamber 8, and the bottom of outer tank body 7 is additionally provided with and heating chamber 8
Cold and hot matchmaker's inlet pipe 14 of connection, can each lead into and discharge cold and hot matchmaker, with to anti-by cold and hot matchmaker's inlet pipe 14 and cold and hot matchmaker's outlet pipe 4
Answer and multiple pillars 6 are additionally provided with the inner chamber temperature adjustment of chamber 19, the heating chamber 8, pillar 6 is albronze cylinder, the one of pillar 6
End is fixed on the outer wall of inner tank body 9, and the other end of pillar 6 is fixed on the inwall of outer tank body 7, can both have been carried by pillar 6
The stability between outer tank body 7 and inner tank body 9 is risen, the enrichment of heat is beneficial to again so that the temperature change of reaction chamber 19 is permanent steady.
The middle part of the reaction chamber 19 is provided with agitating shaft 17 vertically, and the crown center of outer tank body 7 is provided with to be connected with agitating shaft 17
The motor 3 connect, agitating shaft 17 is that sealing rotation is connected with outer tank body 7 and inner tank body 9, and agitating shaft 17 can be driven by motor 3
Rotate, the middle part of the reaction chamber 19 includes the He of puddler 24 in being provided with rabbling mechanism 16, rabbling mechanism 16 on agitating shaft 17
Agitating plate 22, the both sides of agitating shaft 17 are mounted on agitating plate 22, and agitating plate 22 is semicircular plate, if being offered on agitating plate 22
Dry second through hole 23, the outside of agitating plate 22 is provided with some puddlers 24, and the puddler 24 is horizontally disposed with, and puddler 24 is with stirring
Mix plate 22 in the same plane, coordinating by agitating plate 22 and puddler 24 can be to material stirring, and the second through hole 23 is beneficial to will
Grease, catalyst refinement separation, have further speeded up the fusion haptoreaction of grease and catalyst, have improved the speed of esterification reaction
Degree and reaction mass, the upside of the rabbling mechanism 16 are provided with water conservancy diversion web plate 18, and the water conservancy diversion web plate 18 is that middle part is downwardly projecting
Pyramidal structure, the outer ring of water conservancy diversion web plate 18 and the inwall of inner tank body 9 are in one 3~5cm gap, and the middle part of water conservancy diversion web plate 18 is opened
Provided with pod apertures 21, provided with multiple support bars 20 being connected with agitating shaft 17 in pod apertures 21, the support bar 20 is circumferential
Three are uniformly provided with, fixation, the downside stirring of the rabbling mechanism 16 can be supported to water conservancy diversion web plate 18 by support bar 20
The lower end of axle 17 is provided with material scraping plate 12, and the material scraping plate 12 is that some the are offered on the recessed arc in middle part, material scraping plate 12
One through hole 11, the downside of material scraping plate 12 is provided with the screen pack 15 being engaged with material scraping plate 12, the outer ring of screen pack 15 with it is interior
The inwall of tank body 9 is fixedly connected, and the middle part connection of the screen pack 15 is provided with circulation pipe 5, and circulation pipe 5 is provided with circulating pump
10, the other end of circulation pipe 5 is located in the reaction chamber 19 of the upside of water conservancy diversion web plate 18, can be by thing by controlling circulating pump 10 to work
Material circulates extraction by circulation pipe 5, lifts ratio defective product.
In embodiment, the feed pipe 1, the outlet of catalyst tube 2 and circulation pipe 5 are located above the outside of pod apertures 21,
It may be such that material is first dropped on water conservancy diversion web plate 18, then centrifuged away or flowed down by pod apertures 21 by water conservancy diversion web plate 18.
In embodiment, the first through hole 11, the second through hole 23 and pod apertures 21 are circular port or regular polygon hole.
In embodiment, regulating valve is equipped with cold and hot matchmaker's inlet pipe 14 and cold and hot matchmaker's outlet pipe 4（It is not shown）, can carry out cold
Heating agent is adjusted.
The high yield biodiesel prepares reactor, in addition to the PLC controls for being controlled to motor 3, circulating pump 10
Device（It is not shown）, grease and catalyst can be added by feed pipe 1 and catalyst tube 2, motor 3 can drive agitating shaft 17 to rotate,
Grease and catalyst are dropped on water conservancy diversion web plate 18, can directly be filtered lower or be centrifuged from the outer ring of water conservancy diversion web plate 18 by water conservancy diversion web plate 18
Throw away or flowed down from pod apertures 21, merged beneficial to contact of the grease with catalyst, by the agitating plate 22 of rabbling mechanism 16 and stirred
Mixing that bar 24 coordinates can be to material stirring, and the second through hole 23 is beneficial to separate grease, catalyst refinement, further speeded up grease and
The fusion haptoreaction of catalyst, improves the speed and reaction mass of esterification reaction, by the material scraping plate 12 of rotation and thereon
The first through hole 11 opened up is beneficial to material under the filter of screen pack 15, and the defective material on screen pack 15 can be dropped into circulation pipe 5,
Circulation conveying reaction is carried out by circulating pump 10, the raw material availability of biodiesel is lifted；By cold and hot matchmaker's inlet pipe 14 to heating
Cold and hot matchmaker is passed through in chamber 8, the temperature beneficial to reaction is adapted to, and cold and hot matchmaker can be discharged by cold and hot matchmaker's outlet pipe 4；Both may be used by pillar 6
To lift the stability between outer tank body 7 and inner tank body 9, the enrichment of heat is beneficial to again so that the temperature change of reaction chamber 19 is permanent
Surely；The apparatus structure is novel, and material mixing Quick uniform in reactor, raw material availability is high, and yield is higher.
It is obvious to a person skilled in the art that the invention is not restricted to the details of above-mentioned one exemplary embodiment, Er Qie
In the case of without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter
From the point of view of which point, embodiment all should be regarded as exemplary, and be nonrestrictive, the scope of the present invention is by appended power
Profit is required rather than described above is limited, it is intended that all in the implication and scope of the equivalency of claim by falling
Change is included in the present invention.Any reference in claim should not be considered as to the claim involved by limitation.
The above is only the preferred embodiment of the present invention, it is noted that for those skilled in the art, not
On the premise of departing from present inventive concept, several modifications and improvements can also be made, these should also be considered as the protection model of the present invention
Enclose, these effects and practical applicability for implementing all without the influence present invention.
Claims (8)
1. a kind of high yield biodiesel prepares reactor, including outer tank body（7）And inner tank body（9）, it is characterised in that the inner canister
Body（9）Located at outer tank body（7）Inner side, inner tank body（9）And outer tank body（7）Between space be heating chamber（8）, inner tank body（9）
Inner space be reaction chamber（19）, the outer tank body（7）Top be respectively equipped with and reaction chamber（19）The feed pipe of connection（1）
And catalyst tube（2）, the outer tank body（7）Bottom in the middle of be provided with and reaction chamber（19）The drainage conduit of connection（13）, it is described outer
Tank body（7）Top be additionally provided with and heating chamber（8）Cold and hot matchmaker's outlet pipe of connection（4）, outer tank body（7）Bottom be additionally provided with and heat
Chamber（8）Cold and hot matchmaker's inlet pipe of connection（14）, the heating chamber（8）Inside it is additionally provided with multiple pillars（6）, the reaction chamber（19）In
Portion is provided with agitating shaft vertically（17）, outer tank body（7）Crown center be provided with and agitating shaft（17）The motor of connection（3）, agitating shaft
（17）With outer tank body（7）And inner tank body（9）It is that sealing rotates connection, the reaction chamber（19）Middle part in agitating shaft（17）On
Rabbling mechanism is installed（16）, rabbling mechanism（16）Including puddler（24）And agitating plate（22）, agitating shaft（17）Both sides it is equal
Agitating plate is installed（22）, agitating plate（22）For semicircular plate, agitating plate（22）On offer some second through holes（23）, stirring
Plate（22）Outside be provided with some puddlers（24）, puddler（24）It is horizontally disposed, puddler（24）With agitating plate（22）It is located at
On same plane, the rabbling mechanism（16）Upside be provided with water conservancy diversion web plate（18）, water conservancy diversion web plate（18）It is downwardly projecting for middle part
Pyramidal structure, water conservancy diversion web plate（18）Outer ring and inner tank body（9）Inwall be in one 3~5cm gap, water conservancy diversion web plate（18）'s
Middle part offers pod apertures（21）, pod apertures（21）It is interior to be provided with multiple and agitating shaft（17）The support bar being connected（20）, institute
State rabbling mechanism（16）Downside agitating shaft（17）Lower end is provided with material scraping plate（12）, material scraping plate（12）On offer some first
Through hole（11）, material scraping plate（12）Downside be provided with and material scraping plate（12）The screen pack being engaged（15）, screen pack（15）'s
Outer ring and inner tank body（9）Inwall be fixedly connected, the screen pack（15）Middle part connection be provided with circulation pipe（5）, circulation pipe
（5）It is provided with circulating pump（10）, circulation pipe（5）The other end be located at water conservancy diversion web plate（18）The reaction chamber of upside（19）It is interior.
2. high yield biodiesel according to claim 1 prepares reactor, it is characterised in that the outer tank body（7）With it is interior
Tank body（9）It is the totally-enclosed cylindrical tube structure that two ends are protruded to outer arcuate.
3. high yield biodiesel according to claim 1 prepares reactor, it is characterised in that the pillar（6）For copper aluminium
Alloy cylinder, pillar（6）One end be fixed on inner tank body（9）Outer wall on, pillar（6）The other end be fixed on outer tank body（7）
Inwall on.
4. high yield biodiesel according to claim 1 prepares reactor, it is characterised in that the support bar（20）It is circumferential
It is uniformly provided with three.
5. high yield biodiesel according to claim 1 prepares reactor, it is characterised in that the material scraping plate（12）For in
The recessed arc of subordinate.
6. high yield biodiesel according to claim 1 prepares reactor, it is characterised in that the feed pipe（1）, catalysis
Agent pipe（2）And circulation pipe（5）Outlet be located at pod apertures（21）Outside above.
7. high yield biodiesel according to claim 1 prepares reactor, it is characterised in that the first through hole（11）、
Second through hole（23）And pod apertures（21）It is circular port or regular polygon hole.
8. high yield biodiesel according to claim 1 prepares reactor, it is characterised in that cold and hot matchmaker's inlet pipe（14）
With cold and hot matchmaker's outlet pipe（4）On be equipped with regulating valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710557884.4A CN107126918A (en) | 2017-07-10 | 2017-07-10 | A kind of high yield biodiesel prepares reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710557884.4A CN107126918A (en) | 2017-07-10 | 2017-07-10 | A kind of high yield biodiesel prepares reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107126918A true CN107126918A (en) | 2017-09-05 |
Family
ID=59737369
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710557884.4A Withdrawn CN107126918A (en) | 2017-07-10 | 2017-07-10 | A kind of high yield biodiesel prepares reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107126918A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108911401A (en) * | 2018-07-24 | 2018-11-30 | 安徽电信工程有限责任公司 | A kind of energy-efficient processing system of domestic sewage in rural areas |
| CN109550474A (en) * | 2018-11-27 | 2019-04-02 | 高美珍 | A kind of industrial chemicals reaction kettle based on convection current collision stirring technique |
| CN109647313A (en) * | 2017-10-12 | 2019-04-19 | 天津市易泰柯自动控制设备有限公司 | A kind of liquid hazardous chemicals hair answers kettle |
| CN111790288A (en) * | 2020-07-21 | 2020-10-20 | 金华职业技术学院 | Preparation method and equipment of magnetic nano composite material |
| CN112473597A (en) * | 2020-11-06 | 2021-03-12 | 郑员锋 | Saturated polyester resin production equipment for powder coating and production method thereof |
-
2017
- 2017-07-10 CN CN201710557884.4A patent/CN107126918A/en not_active Withdrawn
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109647313A (en) * | 2017-10-12 | 2019-04-19 | 天津市易泰柯自动控制设备有限公司 | A kind of liquid hazardous chemicals hair answers kettle |
| CN108911401A (en) * | 2018-07-24 | 2018-11-30 | 安徽电信工程有限责任公司 | A kind of energy-efficient processing system of domestic sewage in rural areas |
| CN109550474A (en) * | 2018-11-27 | 2019-04-02 | 高美珍 | A kind of industrial chemicals reaction kettle based on convection current collision stirring technique |
| CN111790288A (en) * | 2020-07-21 | 2020-10-20 | 金华职业技术学院 | Preparation method and equipment of magnetic nano composite material |
| CN111790288B (en) * | 2020-07-21 | 2022-08-09 | 金华职业技术学院 | Preparation method and equipment of magnetic nano composite material |
| CN112473597A (en) * | 2020-11-06 | 2021-03-12 | 郑员锋 | Saturated polyester resin production equipment for powder coating and production method thereof |
| CN112473597B (en) * | 2020-11-06 | 2022-08-02 | 河南省中泰石化有限公司 | Saturated polyester resin production equipment for powder coating and production method thereof |
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Application publication date: 20170905 |