CN201037134Y - Tubular reactor with static mixing element and biological diesel oil continuous reactor - Google Patents
Tubular reactor with static mixing element and biological diesel oil continuous reactor Download PDFInfo
- Publication number
- CN201037134Y CN201037134Y CNU200720089873XU CN200720089873U CN201037134Y CN 201037134 Y CN201037134 Y CN 201037134Y CN U200720089873X U CNU200720089873X U CN U200720089873XU CN 200720089873 U CN200720089873 U CN 200720089873U CN 201037134 Y CN201037134 Y CN 201037134Y
- Authority
- CN
- China
- Prior art keywords
- static mixing
- mixing element
- reactor
- tubular reactor
- heating unit
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a tubular reactor with static hybrid elements consisting of static hybrid elements arranged in the middle of a tube body and heating elements arranged outside the tube body. The heating elements are sleeve pipes which are arranged outside the tube body and work as a heating medium or resistance wires of an out-sleeved ceramic ring of a ceramic tube. The static hybrid elements are Kenics static hybrid elements or GK static hybrid elements. A biodiesel successive reaction device comprises a first-order reactor and a second-order reactor which are connected in series, wherein, the second-order reactor is connected with a separator; the front of the first-order reactor is connected with the tubular reactor with static hybrid elements which consists of static hybrid elements arranged in the middle of a tube body and heating elements arranged outside the tube body. The utility model manufactures biodiesel and has the advantages of simple equipment, low investment, low energy consumption and good effect.
Description
Technical field
The utility model belongs to production of biodiesel device technique field, particularly a kind of tubular reactor and biofuel continuous reaction apparatus that has static mixing element.
Background technology
Along with continuous progress in science and technology, human more and more higher to the degree of dependence of the energy, cause the petrochemical industry resource to peter out.Biofuel can be used as the substitute of traditional petrifaction diesel, and combustionproperty is suitable, and sulfur-bearing, oxygen level are high and have biodegradability, can significantly reduce environmental pollution, have excellent environmental-protecting performance.Thereby, wide application prospect is arranged as a kind of novel renewable energy.
Existing biofuel reaction unit mostly is intermittently stirring-type greatly, and mixed effect is good inadequately, and energy consumption is very high.CN1740273A adopts coil pipe type reactor to realize continuous production, but before alcohol and grease enter tubular reactor, is preheating to the low-temperature values that sets by a cryogenic thermostat preheater earlier.Alcohol and grease feed in the tubular reactor that is heated by a high temperature constant temperature process furnace after mixing tank mixes again, are elevated to required high temperature values.This method need adopt special well heater and mixing tank to carry out the heating of alcohol oil, mix, and has increased facility investment.CN1743416A adopts two sections tubular reactors, all was added with interchanger and carries out heat exchange to improve temperature before two sections tubular reactors.This method need adopt special interchanger to carry out heat exchange.
The utility model content
The utility model purpose is to provide a kind of tubular reactor and biofuel continuous reaction apparatus of the band static mixing element that heating edge is reacted while mixing.
For reaching above-mentioned purpose, the utility model adopts following technical scheme: the tubular reactor of band static mixing element constitutes by being located at body intermediary static mixing element and being located at the outer heating unit of body.
Heating unit is to be located at the sleeve pipe that body is outer, supply heating medium to pass through.
Heating unit be located at that body is outer, the resistance wire of outer cotton up to ring or porcelain tube.
Static mixing element is Kenics static mixing element or GK static mixing element.
The biofuel continuous reaction apparatus, comprise mutual placed in-line A reactor and second reactor, second reactor connects separator, the tubular reactor of tape splicing static mixing element before the A reactor, the tubular reactor of band static mixing element constitutes by being located at body intermediary static mixing element and being located at the outer heating unit of body.
Heating unit is to be located at the sleeve pipe that body is outer, supply heating medium to pass through.
Heating unit be located at that body is outer, the resistance wire of outer cotton up to ring or porcelain tube.
Static mixing element is Kenics static mixing element or GK static mixing element.
In the utility model, tubular reactor constitutes by being located at body intermediary static mixing element and being located at the outer heating unit of body, can be single hose or telescoping, can or be welded to connect by flange between each section, it is spiral that profile can be coil pipe type, oval coil tube type, Long Circle.Static mixing element is known for those skilled in the art, be a series of structural similitudies of in body, placing, by certain regularly arranged stationary element, when fluid flows through, rely on the fluid self kinetic energy, realize constantly cutting, be out of shape, be shifted and converge, can realize the fluidic thorough mixing, energy consumption is low, compact construction, manufacturing is easy for installation, floor space is little, running cost is low.Static mixing element can be Kenics static cell, GK static cell.Heating unit is to be located at the body sleeve pipe outer, that pass through for heating medium or the resistance wire of outer cotton up to ring or porcelain tube.This tubular reactor can make raw materials such as grease and low first alcohol while mixing heating edge react, mix, the level of response height, can realize the segmentation gradient-heated, also can realize not having gradient-heated.
The biofuel continuous reaction apparatus is composed in series by the tubular reactor that has static mixing element and A reactor, second reactor and separator, thermal source can be steam, warm air, stack gas, fused salt, thermal oil or; A reactor, second reactor and separator are conventional equipment, and equipment is simple, invest for a short time, and energy consumption is low.Be applicable to and utilize grease, pure production biofuel and harmonic biodiesel.When being used for harmonic biodiesel, only adopt tubular reactor to get final product.The utility model manufacturing is simple, and special heating, mixing device need be provided, and is suitable for industrial-scale production.
Description of drawings
Fig. 1 is a biofuel continuous reaction apparatus structural representation.Wherein, horizontal arrow is the material movement direction, and perpendicular arrow is steam or wet goods flow direction.
Embodiment
In embodiment 2, the present embodiment, the tubular reactor of band static mixing element is oval coil tube type, and static mixing element 2 is the Kenics static mixing element, and the heating medium in the sleeve pipe is a thermal oil.Other are with embodiment 1.
In embodiment 3, the present embodiment, tubular reactor is a sector boss round screw thread tubular reactor, and static mixing element 2 is the GK static mixing element.Heating medium in the sleeve pipe is a fused salt.Other are with embodiment 1.
In embodiment 4, the present embodiment, heating unit 1 is the resistance wire of cotton up to ring or porcelain tube.Other are with embodiment 1.
Claims (8)
1. the tubular reactor of band static mixing element is characterized in that, constitutes by being located at body intermediary static mixing element and being located at the outer heating unit of body.
2. the tubular reactor of band static mixing element as claimed in claim 1 is characterized in that, heating unit is to be located at the sleeve pipe that body is outer, supply heating medium to pass through.
3. the tubular reactor of band static mixing element as claimed in claim 1 is characterized in that, heating unit be located at that body is outer, the resistance wire of outer cotton up to ring or porcelain tube.
4. as the tubular reactor of claim 1,2 or 3 described band static mixing elements, it is characterized in that static mixing element is Kenics static mixing element or GK static mixing element.
5. biofuel continuous reaction apparatus, comprise mutual placed in-line A reactor and second reactor, second reactor connects separator, it is characterized in that, the tubular reactor of tape splicing static mixing element before the A reactor, the tubular reactor of band static mixing element constitutes by being located at body intermediary static mixing element and being located at the outer heating unit of body.
6. biofuel continuous reaction apparatus as claimed in claim 5 is characterized in that, heating unit is to be located at the sleeve pipe that body is outer, supply heating medium to pass through.
7. biofuel continuous reaction apparatus as claimed in claim 5 is characterized in that, heating unit be located at that body is outer, the resistance wire of outer cotton up to ring or porcelain tube.
8. as claim 5,6 or 7 described biofuel continuous reaction apparatus, it is characterized in that static mixing element is Kenics static mixing element or GK static mixing element.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200720089873XU CN201037134Y (en) | 2007-04-02 | 2007-04-02 | Tubular reactor with static mixing element and biological diesel oil continuous reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200720089873XU CN201037134Y (en) | 2007-04-02 | 2007-04-02 | Tubular reactor with static mixing element and biological diesel oil continuous reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201037134Y true CN201037134Y (en) | 2008-03-19 |
Family
ID=39209646
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU200720089873XU Expired - Fee Related CN201037134Y (en) | 2007-04-02 | 2007-04-02 | Tubular reactor with static mixing element and biological diesel oil continuous reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201037134Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101935593A (en) * | 2010-09-07 | 2011-01-05 | 徐荣江 | Method for preparing biodiesel by adopting supercritical methanol continuous process |
-
2007
- 2007-04-02 CN CNU200720089873XU patent/CN201037134Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101935593A (en) * | 2010-09-07 | 2011-01-05 | 徐荣江 | Method for preparing biodiesel by adopting supercritical methanol continuous process |
| CN101935593B (en) * | 2010-09-07 | 2012-10-03 | 徐荣江 | Method for preparing biodiesel by adopting supercritical methanol continuous process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105623861B (en) | A kind of glycerine esterification reaction unit | |
| CN201581065U (en) | Complete apparatus for fast producing bio-diesel | |
| CN204224252U (en) | A kind of methanol oxidation heat supply device for producing hydrogen | |
| CN201400651Y (en) | Combination preheater of oil and air in the production of carbon ink | |
| CN201037134Y (en) | Tubular reactor with static mixing element and biological diesel oil continuous reactor | |
| CN100503533C (en) | Methyl esterification in biologic diesel oil production and methanol continuously purification device | |
| CN208916818U (en) | A kind of iron powder hydrogen production reaction furnace and device | |
| CN101881553A (en) | Catalytic combustion heat recovery system and method | |
| CN204454569U (en) | A kind of cascading double-sided how snakelike microchannel reforming hydrogen-preparation reactor | |
| CN105907481A (en) | Alternating serial reaction device for producing biodiesel from high-pressure gas-phase methanol | |
| CN203310268U (en) | Waste heat utilization device of tantalum-niobium oxide calcining device | |
| CN114890383A (en) | Skid-mounted methanol hydrogen production and filling integrated device | |
| CN204897850U (en) | Living beings pyrolysis gas dust removal heat exchanger | |
| CN201037139Y (en) | Device for producing methyl esterification biological diesel oil and continuously purifying methanol | |
| CN204841658U (en) | Gas phase reaction prepares biodiesel's device in succession | |
| CN112370947A (en) | Energy-concerving and environment-protective type nitrile rubber reforms transform waste gas waste heat recovery and utilizes device | |
| CN107236597B (en) | Biodiesel transesterification real-time dynamic separation continuous reaction system and application thereof | |
| CN202356095U (en) | Enamel reaction kettle | |
| CN201740358U (en) | Drying tower system | |
| CN206660962U (en) | A kind of carbonyl sulfide hydrolysis device | |
| CN205222682U (en) | Combustible gas generating device | |
| CN110079351A (en) | It is a kind of using helix tube moving-burden bed reactor as the biomass through pyrolysis production technology of core | |
| CN205062012U (en) | Ultrasonic wave serialization biodiesel fuel production device | |
| CN201883076U (en) | High-condensation point biodiesel catalytic cracking device | |
| CN203513615U (en) | Efficient combined type shift gas-semiwater gas heat exchanger |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080319 Termination date: 20130402 |