CN215559011U - Micro-interface oxidation system for preparing hydrogen peroxide - Google Patents
Micro-interface oxidation system for preparing hydrogen peroxide Download PDFInfo
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- CN215559011U CN215559011U CN202121636018.2U CN202121636018U CN215559011U CN 215559011 U CN215559011 U CN 215559011U CN 202121636018 U CN202121636018 U CN 202121636018U CN 215559011 U CN215559011 U CN 215559011U
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- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 78
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 title claims abstract description 68
- 230000003647 oxidation Effects 0.000 title claims abstract description 33
- 239000007788 liquid Substances 0.000 claims abstract description 67
- 239000000839 emulsion Substances 0.000 claims abstract description 49
- PYKYMHQGRFAEBM-UHFFFAOYSA-N anthraquinone Natural products CCC(=O)c1c(O)c2C(=O)C3C(C=CC=C3O)C(=O)c2cc1CC(=O)OC PYKYMHQGRFAEBM-UHFFFAOYSA-N 0.000 claims abstract description 28
- 150000004056 anthraquinones Chemical class 0.000 claims abstract description 26
- 239000007789 gas Chemical class 0.000 claims abstract description 23
- 239000007791 liquid phase Substances 0.000 claims abstract description 21
- 239000012071 phase Substances 0.000 claims abstract description 17
- 239000000203 mixture Substances 0.000 claims abstract description 15
- 239000010902 straw Substances 0.000 claims abstract description 4
- 238000006243 chemical reaction Methods 0.000 claims description 27
- 230000000694 effects Effects 0.000 claims description 14
- 230000002708 enhancing effect Effects 0.000 claims 1
- 239000001301 oxygen Substances 0.000 abstract description 18
- 229910052760 oxygen Inorganic materials 0.000 abstract description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 17
- 238000000034 method Methods 0.000 description 19
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- 230000008569 process Effects 0.000 description 8
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- SJEBAWHUJDUKQK-UHFFFAOYSA-N 2-ethylanthraquinone Chemical compound C1=CC=C2C(=O)C3=CC(CC)=CC=C3C(=O)C2=C1 SJEBAWHUJDUKQK-UHFFFAOYSA-N 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 238000000605 extraction Methods 0.000 description 4
- 238000005984 hydrogenation reaction Methods 0.000 description 4
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- YEVQZPWSVWZAOB-UHFFFAOYSA-N 2-(bromomethyl)-1-iodo-4-(trifluoromethyl)benzene Chemical compound FC(F)(F)C1=CC=C(I)C(CBr)=C1 YEVQZPWSVWZAOB-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- -1 alkyl anthraquinone Chemical class 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- HWOWEGAQDKKHDR-UHFFFAOYSA-N 4-hydroxy-6-(pyridin-3-yl)-2H-pyran-2-one Chemical compound O1C(=O)C=C(O)C=C1C1=CC=CN=C1 HWOWEGAQDKKHDR-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
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Abstract
The utility model provides a micro-interface oxidation system for preparing hydrogen peroxide, wherein the micro-interface oxidation system comprises: an oxidation reaction tower; the side surface of the oxidation reaction tower is provided with a liquid phase pipeline for conveying hydrogenated anthraquinone and a gas phase pipeline for conveying air; be provided with in the oxidation reaction tower and mix the micro-interface unit, mix the micro-interface unit and include upper set micro-interface generator and the lower micro-interface generator of putting of upper and lower intercommunication, upper set micro-interface generator and be provided with long and narrow gas-liquid emulsion passageway between the lower micro-interface generator, gas-liquid emulsion passageway is connected with the gas-liquid emulsion export, the gas-liquid emulsion export hug closely in the last lateral wall of putting down micro-interface generator, the top of upper set micro-interface generator is provided with the volume straw that is used for the air entrainment at top in the tower. The micro-interface oxidation system can improve the utilization rate of oxygen, occupies small area and is simple and convenient to operate.
Description
Technical Field
The utility model relates to the field of hydrogen peroxide preparation, in particular to a micro-interface oxidation system for preparing hydrogen peroxide.
Background
Hydrogen peroxide (H)2O2) The aqueous solution is an important inorganic peroxide, has the characteristics of oxidability, bleachability, green and environment-friendly use process and the like, can be applied to the fields of fabric and paper pulp decoloration, chemical synthesis, wastewater treatment, medical treatment, metallurgy, military industry, food processing and the like, and can be used as an oxidant, a bleaching agent, a disinfectant, a polymer initiator, a cross-linking agent, a propellant and the like. With the stricter environmental protection regulations, the production capacity of products such as propylene oxide, green caprolactam and the like produced by a hydrogen peroxide direct oxidation process (HPPO process) is increased, so that H is generated2O2The market demand of (2) is strong.
The production method of hydrogen peroxide includes anthraquinone method, electrolytic method, isopropanol oxidation method, inorganic reaction method, and direct hydrogen-oxygen synthesis method. Among them, the anthraquinone process is the mainstream method for producing hydrogen peroxide at home and abroad at present.
The anthraquinone process of producing hydrogen peroxide is to use 2-Ethyl Anthraquinone (EAQ) as carrier and heavy Arene (AR) and trioctyl phosphate (TOP) as mixed solvent to compound solution with certain composition, and under the catalysis of Pd or Ni catalyst, alkyl anthraquinone is catalytically hydrogenated and air oxidized alternately to produce hydrogen peroxide extracted with water to form coarse hydrogen peroxide for reuse. However, in the existing process, the utilization rate of oxygen in the oxidation process is low, so that the yield of the prepared hydrogen peroxide is low.
In view of the above, the present invention is particularly proposed.
SUMMERY OF THE UTILITY MODEL
The first purpose of the utility model is to provide a micro-interface oxidation system for preparing hydrogen peroxide, wherein a mixed micro-interface unit is arranged in an oxidation reaction tower, so that air is crushed into micro-bubbles before the air and hydrogenated anthraquinone are subjected to oxidation reaction, and the phase boundary mass transfer area between the air and the hydrogenated anthraquinone is increased, thereby solving the problems of low oxygen utilization rate and low product yield caused by the fact that the air and the hydrogenated anthraquinone cannot be fully mixed in the oxidation reaction tower in the prior art.
The second purpose of the utility model is to provide a reaction method for preparing hydrogen peroxide by adopting a micro-interface oxidation system, the hydrogen peroxide obtained by the reaction has high purity and wide application, the application range of the hydrogen peroxide is improved, and the method is worthy of wide popularization and application.
In order to achieve the above purpose of the present invention, the following technical solutions are adopted:
the utility model provides a micro-interface oxidation system for preparing hydrogen peroxide, which comprises: an oxidation reaction tower; the side surface of the oxidation reaction tower is provided with a liquid phase pipeline for conveying hydrogenated anthraquinone and a gas phase pipeline for conveying air;
be provided with in the oxidation reaction tower and mix the micro-interface unit, mix the micro-interface unit and include upper set micro-interface generator and the lower set micro-interface generator of upper and lower intercommunication, upper set micro-interface generator and be provided with long and narrow gas-liquid emulsion passageway between the lower set micro-interface generator, gas-liquid emulsion passageway is connected with the gas-liquid emulsion export, the gas-liquid emulsion export hug closely in the last lateral wall of lower set micro-interface generator, the top of upper set micro-interface generator is provided with the volume straw that is used for the air entrainment at top in the tower.
In the micro-interface oxidation system, the raw materials are hydrogenated anthraquinone and air, the hydrogenated anthraquinone is a product obtained by hydrogenation through a hydrogenation tower, generally in actual operation, working solution containing anthraquinone derivatives and a catalyst are firstly conveyed into the hydrogenation tower, meanwhile, hydrogen is conveyed into the hydrogenation tower to generate a mixture containing 2-ethyl hydrogen anthraquinone solution, the mixture is conveyed into an oxidation reaction tower after being filtered and cooled, a gas-liquid emulsion is formed in the oxidation reaction tower and the air subjected to micro-interface dispersion and crushing, oxidation reaction is carried out to generate a mixture containing 2-ethyl anthraquinone and hydrogen peroxide, the mixture containing 2-ethyl anthraquinone and hydrogen peroxide is conveyed to an extraction tower, the mixture containing 2-ethyl anthraquinone and hydrogen peroxide and pure water are extracted in the extraction tower, and the product obtained after extraction is hydrogen peroxide.
In the scheme of the utility model, the mixed micro-interface unit is arranged in the oxidation reaction tower, so that the utilization rate of air is improved, and the yield of hydrogen peroxide is further improved, the mixed micro-interface unit combines the micro-interface generators together through a specific structure, the mixed micro-interface unit comprises an upper micro-interface generator and a lower micro-interface generator, the micro-interface generators and the lower micro-interface generator are required to be combined and communicated with each other up and down and are not arranged independently, so that the arrangement is to improve the firmness of the whole micro-interface unit, the space in the oxidation reaction tower is narrow, if the micro-interface generators are arranged too dispersed, the normal work of the oxidation reaction tower can be influenced, in addition, the distance of each micro-interface generator is shortened due to the integral structure, the mutual cooperation capability among all parts is enhanced, and after bubbles crushed by the micro-interfaces collide with each other, thereby improving the dispersion crushing effect. The collision, dispersion and crushing of the gas-liquid emulsion are enhanced through the mutually communicated channels.
In addition, in the scheme of the utility model, the upper-mounted micro-interface generator and the lower-mounted micro-interface generator are communicated up and down through a gas-liquid emulsion channel, the gas-liquid emulsion channel is directly communicated with a gas-liquid emulsion outlet, the gas-liquid emulsion outlet is an outlet of gas-liquid emulsion formed after the upper-mounted micro-interface generator is dispersed and crushed, because the upper part in the oxidation reaction tower belongs to a mixing zone and the lower part in the oxidation reaction tower belongs to a violent reaction zone, materials on the upper part are mixed stably, the reaction on the lower part is violent, so that the gas-liquid emulsion channel can be slightly longer to improve the reaction effect, power is provided for materials discharged from the gas-liquid emulsion outlet through the guiding function of the gas-liquid emulsion channel, and the gas-liquid emulsion outlet is just attached to the upper side wall of the lower-mounted micro-interface generator, so that the gas-liquid emulsion discharged from the outlet immediately acts with the lower-mounted micro-interface generator, improving the dispersion crushing effect. Although not explicitly shown in the figures, the specific structure of the gas-liquid emulsion channel is clear from the text of the present invention.
In addition, this gas-liquid emulsion export can set up to the straight tube shape along the horizontal direction, can also set up to the pipe of bending for 90, and the mouth of pipe is perpendicular up or perpendicular down, and the horizontal direction is direct injection just away, and perpendicular up or perpendicular down direction is equivalent to having set up 180 back bending in the exit to promote the circulation energy of gas-liquid emulsion more, drive the material that is located the mixing effect difference on upper portion and carry out the backmixing and breakage again. The best mode can be designed into a shape that the pipe orifice is discharged towards a plurality of directions, particularly after the dispersed and broken bubbles of the micro-interface generator at the lower part are discharged from the micropores of the wall surface, the bubbles just collide with the gas-liquid emulsion discharged from the gas-liquid emulsion outlet immediately, and the gas-liquid emulsion outlet can completely cover the micropores of the wall surface of the underlying micro-interface generator.
Preferably, in the hybrid micro-interface unit of the utility model, the upper micro-interface generator is a gas-liquid linkage micro-interface generator or a hydraulic micro-interface generator, and the lower micro-interface generator is a pneumatic micro-interface generator. The broken gas phase of the pneumatic micro-interface generator is dispersed from the holes on the wall surface and interacts with the gas-liquid emulsion from the upper micro-interface generator, so that the dispersing, fusing and collision effects are enhanced. And the gas-liquid emulsion outlet of the upper group of mixing micro-interface units can be designed to be along the horizontal direction, and the gas-liquid emulsion outlet of the lower group of mixing micro-interface units can be designed to be vertically upward, because the lower part of the mixing micro-interface units belongs to the reaction zone, in order to improve the reaction effect, the sprayed gas-liquid emulsion is upward and then is further improved to be mixed with the material in the upper area, the reaction effect is improved, and further the utilization rate of the raw material is improved.
Preferably, the upper micro-interface generator is located at a position relatively close to the top of the oxidation reaction tower, the lower micro-interface generator is located at a position relatively close to the bottom of the oxidation reaction tower, and the gas-liquid emulsion channel penetrates between the upper micro-interface generator and the lower micro-interface generator. This ensures that the gas-liquid emulsion is sufficiently long and narrow to impart sufficient momentum to the movement in the direction of the underlying micro-interfacial generator.
In the scheme of the utility model, the liquid phase pipeline is generally one and directly extends into the oxidation reaction tower through the side wall of the oxidation reaction tower, the liquid phase pipeline is generally arranged in the middle of the oxidation reaction tower, the gas phase pipeline is preferably divided into a plurality of branches which are respectively communicated with the upper micro-interface generator and the lower micro-interface generator so as to be used for introducing air into the micro-interface generator, when the upper micro-interface generator is a hydraulic micro-interface generator, the gas phase can not be introduced, when the upper micro-interface generator is a gas-liquid linkage micro-interface generator, the gas phase needs to be introduced from the top, and the lower micro-interface generator is generally of a pneumatic type, so the air needs to be directly introduced through the gas phase pipeline which is over expenditure.
Preferably, the gas-liquid linkage type micro-interface generator or the hydraulic type micro-interface generator is connected with a liquid phase circulating pipeline, and the liquid phase circulating pipeline is provided with a circulating pump. The circulating pipeline can continuously suck the gas phase by providing liquid phase power so as to achieve the effect of dispersing and crushing, and the oxygen positioned at the top of the oxidation reaction tower is sucked by the sucking pipe for further utilization.
Preferably, the upper micro-interface generator and the lower micro-interface generator are respectively provided with an individual control valve for switching the working state when the micro-interface generator is blocked. When the lower micro-interface generator is a pneumatic micro-interface generator, pores on the wall surface are easily blocked, so that the lower micro-interface generator can be directly cut out of the system to stop working, the upper micro-interface generator can be used for working, and the pneumatic micro-interface generator can be flushed by utilizing the impulse force of the upper gas-liquid emulsion channel.
It will be appreciated by those skilled in the art that the micro-interface generator used in the present invention is described in the prior patents of the present inventor, such as the patents of application nos. CN201610641119.6, 201610641251.7, CN201710766435.0, CN106187660, CN105903425A, CN109437390A, CN205833127U and CN 207581700U. The detailed structure and operation principle of the micro bubble generator (i.e. micro interface generator) is described in detail in the prior patent CN201610641119.6, which describes that "the micro bubble generator comprises a body and a secondary crushing member, wherein the body is provided with a cavity, the body is provided with an inlet communicated with the cavity, the opposite first end and second end of the cavity are both open, and the cross-sectional area of the cavity decreases from the middle of the cavity to the first end and second end of the cavity; the secondary crushing member is disposed at least one of the first end and the second end of the cavity, a portion of the secondary crushing member is disposed within the cavity, and an annular passage is formed between the secondary crushing member and the through holes open at both ends of the cavity. The micron bubble generator also comprises an air inlet pipe and a liquid inlet pipe. "the specific working principle of the structure disclosed in the application document is as follows: liquid enters the micro-bubble generator tangentially through the liquid inlet pipe, and gas is rotated at a super high speed and cut to break gas bubbles into micro-bubbles at a micron level, so that the mass transfer area between a liquid phase and a gas phase is increased, and the micro-bubble generator in the patent belongs to a pneumatic micro-interface generator.
In addition, the first patent 201610641251.7 describes that the primary bubble breaker has a circulation liquid inlet, a circulation gas inlet and a gas-liquid mixture outlet, and the secondary bubble breaker communicates the feed inlet with the gas-liquid mixture outlet, which indicates that the bubble breakers all need to be mixed with gas and liquid, and in addition, as can be seen from the following drawings, the primary bubble breaker mainly uses the circulation liquid as power, so that the primary bubble breaker belongs to a hydraulic micro-interface generator, and the secondary bubble breaker simultaneously introduces the gas-liquid mixture into an elliptical rotating ball for rotation, thereby realizing bubble breaking in the rotating process, so that the secondary bubble breaker actually belongs to a gas-liquid linkage micro-interface generator. In fact, the micro-interface generator is a specific form of the micro-interface generator, whether it is a hydraulic micro-interface generator or a gas-liquid linkage micro-interface generator, however, the micro-interface generator adopted in the present invention is not limited to the above forms, and the specific structure of the bubble breaker described in the prior patent is only one of the forms that the micro-interface generator of the present invention can adopt.
Furthermore, the prior patent 201710766435.0 states that the principle of the bubble breaker is that high-speed jet flows are used to achieve mutual collision of gases, and also states that the bubble breaker can be used in a micro-interface strengthening reactor to verify the correlation between the bubble breaker and the micro-interface generator; moreover, in the prior patent CN106187660, there is a related description on the specific structure of the bubble breaker, see paragraphs [0031] to [0041] in the specification, and the accompanying drawings, which illustrate the specific working principle of the bubble breaker S-2 in detail, the top of the bubble breaker is a liquid phase inlet, and the side of the bubble breaker is a gas phase inlet, and the liquid phase coming from the top provides the entrainment power, so as to achieve the effect of breaking into ultra-fine bubbles, and in the accompanying drawings, the bubble breaker is also seen to be of a tapered structure, and the diameter of the upper part is larger than that of the lower part, and also for better providing the entrainment power for the liquid phase.
Since the micro-interface generator was just developed in the early stage of the prior patent application, the micro-interface generator was named as a micro-bubble generator (CN201610641119.6), a bubble breaker (201710766435.0) and the like in the early stage, and is named as a micro-interface generator in the later stage along with the continuous technical improvement, and the micro-interface generator in the present invention is equivalent to the micro-bubble generator, the bubble breaker and the like in the prior art, and has different names.
In summary, the micro-interface generator of the present invention belongs to the prior art, although some bubble breakers belong to the type of pneumatic bubble breakers, some bubble breakers belong to the type of hydraulic bubble breakers, and some bubble breakers belong to the type of gas-liquid linkage bubble breakers, the difference between the types is mainly selected according to the different specific working conditions, and in addition, the connection between the micro-interface generator and the reactor and other equipment, including the connection structure and the connection position, is determined according to the structure of the micro-interface generator, which is not limited.
Preferably, both sides of the gas-liquid emulsion channel are provided with grids for improving the reaction effect.
The utility model also provides an oxidation method of the micro-interface oxidation system for preparing hydrogen peroxide, which comprises the following steps:
air is crushed into micro interface and oxidized with hydrogenated anthraquinone to produce hydrogen peroxide
Preferably, the temperature of the oxidation reaction is 35-60 deg.C, preferably 45-55 deg.C, and the reaction pressure is 0.2-0.4MPa, preferably 0.25-0.35 MPa.
The hydrogen peroxide product obtained by the oxidation method has good quality and high yield. And the preparation method has low reaction temperature, greatly reduced pressure and high liquid hourly space velocity, which is equivalent to improving the productivity.
Compared with the prior art, the utility model has the beneficial effects that:
(1) according to the utility model, the mixed micro-interface unit is arranged in the oxidation reaction tower, so that air is crushed into micro-bubbles before the air and the hydrogenated anthraquinone are subjected to oxidation reaction, and the phase boundary mass transfer area between the air and the hydrogenated anthraquinone is increased, thereby solving the problems of low oxygen utilization rate and low product yield caused by the fact that the air and the hydrogenated anthraquinone cannot be fully mixed in the oxidation reaction tower in the prior art;
(2) the oxidation method is simple and convenient to operate, the hydrogen peroxide obtained by the reaction has high purity and wide application, the application range of the hydrogen peroxide is improved, and the method is worthy of wide popularization and application.
Drawings
Various other advantages and benefits will become apparent to those of ordinary skill in the art upon reading the following detailed description of the preferred embodiments. The drawings are only for purposes of illustrating the preferred embodiments and are not to be construed as limiting the utility model. Also, like reference numerals are used to refer to like parts throughout the drawings. In the drawings:
fig. 1 is a schematic structural diagram of a micro-interface oxidation system for preparing hydrogen peroxide according to an embodiment of the present invention.
In the figure:
1-an oxidation reaction tower; 11-liquid phase piping;
12-a gas phase conduit; 13-hybrid micro-interface unit;
131-upper micro-interface generator; 132-a bottom mounted micro-interface generator;
133-gas liquid emulsion channel; 134-a control valve;
135-liquid phase circulation line; 136-a circulation pump;
14-a grid. 15-rolling the straw.
Detailed Description
The technical solutions of the present invention will be clearly and completely described below with reference to the accompanying drawings and the detailed description, but those skilled in the art will understand that the following described embodiments are some, not all, of the embodiments of the present invention, and are only used for illustrating the present invention, and should not be construed as limiting the scope of the present invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention. The examples, in which specific conditions are not specified, were conducted under conventional conditions or conditions recommended by the manufacturer. The reagents or instruments used are not indicated by the manufacturer, and are all conventional products available commercially.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it should be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
In order to more clearly illustrate the technical solution of the present invention, the following description is made in the form of specific embodiments.
Examples
Referring to fig. 1, a micro-interface oxidation system for preparing hydrogen peroxide according to an embodiment of the present invention mainly includes an oxidation reaction tower 1 and a mixed micro-interface unit 13 disposed inside the oxidation reaction tower 1, in the oxidation reaction tower 1, mainly hydrogenated anthraquinone and air are subjected to an oxidation reaction to produce hydrogen peroxide, in order to improve an oxidation effect, grids 14 for improving a reaction effect are disposed on both sides of a gas-liquid emulsion channel, and the grids 14 are disposed in bilateral symmetry.
The mixed micro-interface unit 13 of this embodiment is including connecting the upper-located micro-interface generator 131 and the lower-located micro-interface generator 132 that communicate from top to bottom, the upper-located micro-interface generator 131 and be provided with gas-liquid emulsion passageway 133 between the lower-located micro-interface generator 132, gas-liquid emulsion passageway 133 is connected with the gas-liquid emulsion export, the gas-liquid emulsion export hug closely in the upper side wall of lower-located micro-interface generator 132, the orientation of gas-liquid emulsion export is for the straight tube shape along the horizontal direction or for 90 pipe of bending, and the mouth of pipe is perpendicular up or perpendicular down, and this embodiment is the horizontal direction. The top of the overhead micro-interface generator 131 is provided with a suction pipe 15 for sucking air at the top in the tower.
In the hybrid micro-interface unit 13 according to the embodiment of the present invention, the upper micro-interface generator 131 is a gas-liquid linkage micro-interface generator or a hydraulic micro-interface generator, and the lower micro-interface generator 132 is a pneumatic micro-interface generator. The gas-liquid linkage type micro-interface generator or the hydraulic type micro-interface generator is connected with a liquid phase circulating pipeline 135, a circulating pump 136 is arranged on the liquid phase circulating pipeline 135, and the liquid phase circulating pipeline 135 is used for providing entrainment power for the upper micro-interface generator 131. Through the dispersion and crushing action of the micro-interface generator unit, the oxygen is crushed into micro-bubbles with micron-scale dimensions, and the bubbles are released into the oxidation reaction tower 1, so that the air can be fully contacted with the hydrogenated anthraquinone in a micro-bubble state.
In addition, the upper micro-interface generator 131 and the lower micro-interface generator 132 are respectively provided with an individual control valve 134 for switching an operation state when the micro-interface generator is blocked, the lower micro-interface generator is generally selected to be a pneumatic type so that the blocking is relatively easy to occur, the control valve 134 can be closed, the upper micro-interface generator 131 is only used for performing the individual operation, and the lower micro-interface generator 132 can be flushed when the upper micro-interface generator 131 operates.
The side surface of the oxidation reaction tower 1 is provided with a liquid phase pipeline 11 for conveying hydrogenated anthraquinone and a gas phase pipeline 12 for conveying air, the gas phase pipeline 12 is divided into a plurality of branches which are respectively communicated with an upper micro-interface generator 131 and a lower micro-interface generator 132 for introducing air into the micro-interface generators, and the liquid phase pipeline 11 is a single pipeline and directly extends into the oxidation reaction tower 1 from the middle part of the oxidation reaction tower 1 for conveying hydrogenated anthraquinone raw materials.
The product generated in the oxidation reaction tower 1 goes to the next extraction section, the tail gas is recycled, and the tail gas contains little oxygen, which shows that the oxidation method of the utility model has high oxygen utilization rate.
In order to increase the dispersion and mass transfer effects, an extra micro-interface generator can be additionally arranged, the installation position is not limited actually, the micro-interface generator can be arranged externally or internally, and the micro-interface generator can be arranged on the side wall in the kettle in a relative mode when the micro-interface generator is arranged internally so as to realize the opposite flushing of micro-bubbles from an outlet of the micro-interface generator.
In the above embodiment, the number of the pump bodies is not specifically required, and the pump bodies may be arranged at corresponding positions as required.
In the embodiment, the mass concentration of hydrogenated anthraquinone is 120g/L, the organic solvent is aromatic hydrocarbon, the constant temperature of oxidation heating is 35 ℃, the reaction pressure of an oxidation reaction tower 1 is 0.2MPa, air is introduced at the flow rate of 15L/min, the reaction time is 10min, and after the reaction is finished, sampling is carried out to analyze the conversion rate and the oxygen utilization rate.
Conversion of hydrogenated anthraquinone-100% of reacted feed/raw feed;
the utilization rate of oxygen is 100% of the amount of oxygen already reacted/the amount of oxygen contained in the original air;
and (3) analysis results: the conversion of hydrogenated anthraquinone was 97%, and the utilization of oxygen was 97%.
Example 2
The other operation steps are the same as those of the example 1, except that the constant temperature of the oxidation heating is 45 ℃, the reaction pressure of the oxidation reaction tower 1 is 0.25MPa, and the analysis result is as follows: the conversion of hydrogenated anthraquinone was 96% and the utilization of oxygen was 96%.
Example 3
The other operation steps are the same as those of the example 1, except that the constant temperature of the oxidation heating is 55 ℃, the reaction pressure of the oxidation reaction tower 1 is 0.35MPa, and the analysis result is as follows: the conversion of hydrogenated anthraquinone was 96% and the utilization of oxygen was 96%.
Comparative example 1
The other operation steps are the same as those in example 1, except that the mixed micro-interface unit 13 is not added, and the analysis result is as follows: the conversion of hydrogenated anthraquinone was 90% and the utilization of oxygen was 90%.
Comparative example 2
The other operating steps are identical to those of example 1, except that the hybrid micro-interface unit 13 is replaced by a single micro-interface generator of the pneumatic type, the results of the analysis: the conversion of hydrogenated anthraquinone was 96% and the utilization of oxygen was 96%.
In a word, compared with the micro-interface oxidation system for preparing hydrogen peroxide in the prior art, the micro-interface oxidation system provided by the utility model has the advantages of fewer equipment components, small occupied area, low energy consumption, low cost, high safety, controllable reaction and high raw material conversion rate, is equivalent to providing a micro-interface oxidation system with stronger operability for the field of hydrogen peroxide preparation, and is worthy of wide popularization and application.
Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit the same; while the utility model has been described in detail and with reference to the foregoing embodiments, it will be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; and the modifications or the substitutions do not make the essence of the corresponding technical solutions depart from the scope of the technical solutions of the embodiments of the present invention.
Claims (8)
1. A micro-interface oxidation system for preparing hydrogen peroxide is characterized by comprising: an oxidation reaction tower; the side surface of the oxidation reaction tower is provided with a liquid phase pipeline for conveying hydrogenated anthraquinone and a gas phase pipeline for conveying air;
be provided with in the oxidation reaction tower and mix the micro-interface unit, mix the micro-interface unit and include upper set micro-interface generator and the lower set micro-interface generator of upper and lower intercommunication, upper set micro-interface generator and be provided with long and narrow gas-liquid emulsion passageway between the lower set micro-interface generator, gas-liquid emulsion passageway is connected with the gas-liquid emulsion export, the gas-liquid emulsion export hug closely in the last lateral wall of lower set micro-interface generator, the top of upper set micro-interface generator is provided with the volume straw that is used for the air entrainment at top in the tower.
2. The micro-interfacial oxidation system of claim 1, wherein the gas phase conduit is branched into a plurality of branches, one of which extends into the lower micro-interfacial generator and the other of which extends from a middle portion of the oxidation reactor column.
3. The micro-interfacial oxidation system of claim 1, wherein a grid for enhancing reaction effect is disposed on both sides of the gas-liquid emulsion channel.
4. The system of claim 1, wherein the gas-liquid emulsion outlet is in the form of a straight pipe extending horizontally.
5. The system of claim 1, wherein the outlet of the gas-liquid emulsion is a 90 ° bent pipe with a vertically upward or vertically downward opening.
6. The system of claim 1, wherein the upper micro-interface generator is located relatively close to the top of the oxidation reaction tower, the lower micro-interface generator is located relatively close to the bottom of the oxidation reaction tower, and the gas-liquid emulsion channel extends between the upper micro-interface generator and the lower micro-interface generator.
7. The micro-interface oxidation system according to any one of claims 1 to 6, wherein the upper micro-interface generator and the lower micro-interface generator are respectively provided with a separate control valve for switching the operation state when the micro-interface generator is blocked.
8. The micro-interfacial oxidation system of any one of claims 1 to 6, wherein the overhead micro-interfacial generator is connected to a liquid phase circulation line, and a circulation pump is disposed on the liquid phase circulation line.
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