CN105833561A - Hydrogen peroxide concentration distillation tower - Google Patents
Hydrogen peroxide concentration distillation tower Download PDFInfo
- Publication number
- CN105833561A CN105833561A CN201610385804.7A CN201610385804A CN105833561A CN 105833561 A CN105833561 A CN 105833561A CN 201610385804 A CN201610385804 A CN 201610385804A CN 105833561 A CN105833561 A CN 105833561A
- Authority
- CN
- China
- Prior art keywords
- tower body
- filler
- backflow
- hydrogen peroxide
- hole
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B15/00—Peroxides; Peroxyhydrates; Peroxyacids or salts thereof; Superoxides; Ozonides
- C01B15/01—Hydrogen peroxide
- C01B15/013—Separation; Purification; Concentration
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention relates to a hydrogen peroxide concentration distillation tower which comprises a bottom cone shell, a tower body, a filler support, a filler, a filler press ring, a tank-type liquid distributor, a liquid collector and a top condenser. The hydrogen peroxide concentration distillation tower is characterized by further comprising a supporting frame, a liquid foam capturing filter net, a backflow connecting pipe and a backflow pipe, the liquid foam capturing filter net is arranged at a feeding hole in the tower body through the supporting frame, an impurity discharging hole is formed in the bottom cone shell below the feeding hole, the lower end of the supporting frame is connected on the bottom cone shell below the impurity discharging hole in a downward inclining manner, one end of the backflow pipe is positioned above the tank-type liquid distributor while the other end of the same extends out of the tower body, a backflow hole is formed in the top of the tower body, and one end of the backflow connecting pipe is connected with the backflow hole while the other end of the same is communicated with the backflow pipe. The hydrogen peroxide concentration distillation tower has the advantage of capability of prolonging recycling period of the filler.
Description
Technical field
The present invention relates to a kind of rectifying column, particularly relate to a kind of hydrogen peroxide and concentrate rectifying column.
Background technology
The rectifying column of hydrogen peroxide concentration at present includes for bottom conical shell, tower body, packing support, filler, filler pressing, tank type liquid distributor, liquid header and evaporator overhead condenser;Bottom conical shell is arranged on tower body lower end, is provided with charging hole bottom tower body, and packing support, filler, filler pressing and tank type liquid distributor, liquid header and evaporator overhead condenser are from bottom to top successively set in the tower body above charging hole;This hydrogen peroxide concentrates rectifying column and cannot be separated by impurity in gas-liquid in the course of the work, thus affect filler recycle the cycle.
Summary of the invention
For disadvantages mentioned above, the hydrogen peroxide that it is an object of the invention to provide a kind of cycle that recycles that can improve filler concentrates rectifying column.
The technology contents of the present invention is, a kind of hydrogen peroxide concentrates rectifying column, including for bottom conical shell, tower body, packing support, filler, filler pressing, tank type liquid distributor, liquid header and evaporator overhead condenser;Bottom conical shell is arranged on tower body lower end, is provided with charging hole in tower body lower end, and packing support, filler, filler pressing and tank type liquid distributor, liquid header and evaporator overhead condenser are from bottom to top successively set in the tower body above charging hole;It is characterized in that it also includes a bracing frame, liquid mist eliminating drainage screen, backflow connecting tube and return duct;At the charging hole that liquid mist eliminating drainage screen is mounted in tower body by bracing frame, the bottom conical shell below charging hole is provided with an impurity relief hole;On the downward-sloping bottom conical shell being connected to below impurity relief hole in bracing frame lower end;Return duct end is above tank type liquid distributor, and the return duct other end reaches outside tower body, is provided with a return port at tower body top, and backflow connecting tube one end is connected with return port, and the backflow connecting tube other end connects with return duct.
What the present invention was compared with prior art had is a little: the present invention passes through liquid mist eliminating drainage screen, and tentatively by magazins' layout in gas-liquid, after removing a part of impurity, that can effectively improve filler recycles the cycle;Increase return duct, the tank type liquid distributor that end, tower body top lime set is fed again in tower body is the most repeatedly purified utilization;Improve production efficiency.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Specific embodiment
As it is shown in figure 1, a kind of hydrogen peroxide concentrates rectifying column, including for bottom conical shell 1, tower body 2, packing support 3, filler 4, filler pressing 5, tank type liquid distributor 6, liquid header 7 and evaporator overhead condenser 8;Bottom conical shell 1 is arranged on tower body 2 lower end, be provided with charging hole 2.1 in tower body 2 lower end, packing support 3, filler 4, filler pressing 5 and tank type liquid distributor 6, liquid header 7 and evaporator overhead condenser 8 are from bottom to top successively set in the tower body 2 above charging hole 2.1;It is characterized in that it also includes a bracing frame 9, liquid mist eliminating drainage screen 10, backflow connecting tube 11 and return duct 12;Liquid mist eliminating drainage screen 10 passes through, at the charging hole 2.1 that bracing frame 9 is mounted in tower body 1, the bottom conical shell 1 below charging hole 2.1 to be provided with an impurity relief hole 1.1;On the downward-sloping bottom conical shell 1 being connected to below impurity relief hole 1.1 in bracing frame 9 lower end;Return duct 12 end is above tank type liquid distributor 6, and return duct 12 other end reaches outside tower body 2, is provided with a return port 2.1 at tower body 2 top, and backflow connecting tube 11 one end is connected with return port 2.1, and backflow connecting tube 11 other end connects with return duct 12.
Claims (1)
1. hydrogen peroxide concentrates a rectifying column, including for bottom conical shell, tower body, packing support, filler, filler pressing, tank type liquid distributor, liquid header and evaporator overhead condenser;Bottom conical shell is arranged on tower body lower end, is provided with charging hole in tower body lower end, and packing support, filler, filler pressing and tank type liquid distributor, liquid header and evaporator overhead condenser are from bottom to top successively set in the tower body above charging hole;It is characterized in that it also includes a bracing frame, liquid mist eliminating drainage screen, backflow connecting tube and return duct;At the charging hole that liquid mist eliminating drainage screen is mounted in tower body by bracing frame, the bottom conical shell below charging hole is provided with an impurity relief hole;On the downward-sloping bottom conical shell being connected to below impurity relief hole in bracing frame lower end;Return duct end is above tank type liquid distributor, and the return duct other end reaches outside tower body, is provided with a return port at tower body top, and backflow connecting tube one end is connected with return port, and the backflow connecting tube other end connects with return duct.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610385804.7A CN105833561A (en) | 2016-06-03 | 2016-06-03 | Hydrogen peroxide concentration distillation tower |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610385804.7A CN105833561A (en) | 2016-06-03 | 2016-06-03 | Hydrogen peroxide concentration distillation tower |
Publications (1)
Publication Number | Publication Date |
---|---|
CN105833561A true CN105833561A (en) | 2016-08-10 |
Family
ID=56595638
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610385804.7A Pending CN105833561A (en) | 2016-06-03 | 2016-06-03 | Hydrogen peroxide concentration distillation tower |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105833561A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113082752A (en) * | 2021-04-09 | 2021-07-09 | 云南国润香料制造有限公司 | Sectional type filler rectification device capable of improving eucalyptol extraction efficiency and control system |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102086028A (en) * | 2009-12-07 | 2011-06-08 | 郑国玉 | Concentration method for producing highly-concentrated chemical-grade hydrogen peroxide solution |
CN102161475A (en) * | 2009-11-02 | 2011-08-24 | 郑国玉 | Concentration method in production of hydrogen peroxide by anthraquinone method |
CN204637613U (en) * | 2015-02-13 | 2015-09-16 | 江苏森萱医药化工股份有限公司 | A kind of filler destilling tower |
CN205659429U (en) * | 2016-06-03 | 2016-10-26 | 江阴中南重工有限公司 | Concentrated rectifying column of hydrogen peroxide solution |
-
2016
- 2016-06-03 CN CN201610385804.7A patent/CN105833561A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102161475A (en) * | 2009-11-02 | 2011-08-24 | 郑国玉 | Concentration method in production of hydrogen peroxide by anthraquinone method |
CN102086028A (en) * | 2009-12-07 | 2011-06-08 | 郑国玉 | Concentration method for producing highly-concentrated chemical-grade hydrogen peroxide solution |
CN204637613U (en) * | 2015-02-13 | 2015-09-16 | 江苏森萱医药化工股份有限公司 | A kind of filler destilling tower |
CN205659429U (en) * | 2016-06-03 | 2016-10-26 | 江阴中南重工有限公司 | Concentrated rectifying column of hydrogen peroxide solution |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113082752A (en) * | 2021-04-09 | 2021-07-09 | 云南国润香料制造有限公司 | Sectional type filler rectification device capable of improving eucalyptol extraction efficiency and control system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN205984896U (en) | High -efficient etching machine of PPS | |
CN204736018U (en) | Machine tool cutting fluid recovery unit | |
CN105833561A (en) | Hydrogen peroxide concentration distillation tower | |
CN201164765Y (en) | Wave type gas-liquid separation tank | |
CN205659429U (en) | Concentrated rectifying column of hydrogen peroxide solution | |
CN203610009U (en) | Mechanical gas-liquid separator for chemical industry | |
CN206751443U (en) | A kind of water inlet knockout for multi-effect water distillator evaporator | |
CN201389489Y (en) | Rod mill feed pipe | |
CN205347272U (en) | Separation recovery unit of acetone hydrogenation system isopropyl alcohol | |
CN207243512U (en) | For separating the equipment and system of the carbon dioxide in Methane decarbonization liquid | |
CN207950734U (en) | A kind of vertical foam-resistant extractor | |
CN201978523U (en) | Gas distributing cylinder of packing tower | |
CN201610390U (en) | Water feeding device of integrated oxygen remover | |
CN202427185U (en) | Water catching machine | |
CN206700811U (en) | Integral type reflux column | |
CN202942672U (en) | DMF (Dimethyl Formamide) recovering device in production of synthetic leather | |
CN102826621A (en) | Deoxygenation device for water | |
CN202356093U (en) | Waste heat recovery device for etherification tank | |
CN201988209U (en) | Rectifying tower kettle | |
CN210674722U (en) | Gas-liquid buffer separation device | |
CN215505538U (en) | Olefin device deethanizer with high separation efficiency | |
CN209596577U (en) | One kind efficiently separating evaporator | |
CN204718467U (en) | With the heat exchanger bobbin carriage of separating-purifying structure | |
CN202614010U (en) | Novel condensation recoverer | |
CN202061494U (en) | Liquid drop entrainment separator |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160810 |
|
WD01 | Invention patent application deemed withdrawn after publication |