CN106237656A - The oxime water separation tank produced for diacetylmonoxime - Google Patents

The oxime water separation tank produced for diacetylmonoxime Download PDF

Info

Publication number
CN106237656A
CN106237656A CN201610639709.5A CN201610639709A CN106237656A CN 106237656 A CN106237656 A CN 106237656A CN 201610639709 A CN201610639709 A CN 201610639709A CN 106237656 A CN106237656 A CN 106237656A
Authority
CN
China
Prior art keywords
oxime
baffle
solvent column
tank body
diacetylmonoxime
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
Application number
CN201610639709.5A
Other languages
Chinese (zh)
Inventor
曾曼华
金国洪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
HUBEI XIANLIN CHEMICAL INDUSTRY Co Ltd
Original Assignee
HUBEI XIANLIN CHEMICAL INDUSTRY Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by HUBEI XIANLIN CHEMICAL INDUSTRY Co Ltd filed Critical HUBEI XIANLIN CHEMICAL INDUSTRY Co Ltd
Priority to CN201610639709.5A priority Critical patent/CN106237656A/en
Publication of CN106237656A publication Critical patent/CN106237656A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D17/00Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02Separation of non-miscible liquids
    • B01D17/0208Separation of non-miscible liquids by sedimentation
    • B01D17/0211Separation of non-miscible liquids by sedimentation with baffles

Landscapes

  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Extraction Or Liquid Replacement (AREA)

Abstract

nullThe invention discloses the oxime water separation tank produced for diacetylmonoxime of chemical production device technical field,Including tank body、Solvent column tower body and the drawing liquid water pump being arranged on solvent column tower body intracavity bottom,The inner chamber bottom right side of described tank body is provided with product exit,The intracavity bottom right-to-left of described tank body is respectively arranged with the first vertical baffle plate、Second baffle and third gear plate,The left side of described first baffle plate is provided with pure water inlet,The left side of described second baffle and third gear plate is provided with mixture export,Described mixture export connects connecting tube,The present invention utilizes extractant to be extracted into the dissolubility of oxime in oil phase from oxime aqueous solution by oxime,And be layered by oxime water separation tank,Thus realize the separation of oxime water,And whole apparatus structure is simple,Separation efficiency is high,The mixed liquor separated can also be sent back in solvent column,And then again separate.

Description

The oxime water separation tank produced for diacetylmonoxime
Technical field
The present invention relates to chemical production device technical field, the oxime water separation tank produced particularly for diacetylmonoxime.
Background technology
Diacetylmonoxime is generally colourless or faint yellow oily transparency liquid, and diacetylmonoxime is due to low toxicity, oligosaprobic characteristic, extensively Being applied in the anti skinning agent of coating, ink, paint, meanwhile, diacetylmonoxime is also a class oxygen scavenging chemical, have low toxicity, efficiently, Rapidly, the feature of tool passivation protection effect, additionally, diacetylmonoxime is also the raw material of neutral cross-linking agent.
In the production process of diacetylmonoxime, need oxime water is separated, but existing oxime water separation tank structure be complicated, Oxime water can not be efficiently separated, the inefficiency of separation.
Summary of the invention
It is an object of the invention to provide the oxime water separation tank produced for diacetylmonoxime, to solve above-mentioned background technology carries The problem gone out.
For achieving the above object, the present invention provides following technical scheme: the oxime water separation tank produced for diacetylmonoxime, including Tank body, solvent column tower body and be arranged on the drawing liquid water pump of solvent column tower body intracavity bottom, the inner chamber bottom right side of described tank body sets Be equipped with product exit, vertical the first baffle plate of the intracavity bottom right-to-left of described tank body being provided with respectively, second baffle and Third gear plate, the left side of described first baffle plate is provided with pure water inlet, and the left side of described second baffle and third gear plate is respectively provided with Having mixture export, described pure water inlet and mixture export to be arranged at the intracavity bottom of tank body, described mixture export is even Being connected to connecting tube, the other end of described connecting tube is connected to the right side of water pump, and the left side outfan of described water pump is by pipeline even Being connected on the inner chamber left bottom of solvent column tower body, the inner chamber of described solvent column tower body is provided with agitating device, described solvent column tower The inner chamber right hand top of body is provided with material inlet, and the left side top of described tank body is provided with liquidometer, the inner chamber of described tank body Left bottom connects oxime water inlet pipe, and the other end of described oxime water inlet pipe passes the bottom of solvent column tower body and is connected to take out On the bottom outfan of liquid water pump.
Preferably, the half of a length of second baffle of described first baffle plate, a length of third gear of described second baffle The half of plate.
Preferably, described first baffle plate, second baffle and third gear plate are the intracavity bottom being set in qually spaced in tank body.
Preferably, it is provided with valve in described product exit, pure water inlet and mixture export.
Preferably, described agitating device is impeller, and impeller welds with impeller axle, and impeller axle is arranged on solvent column tower body Front and back on inwall.
Compared with prior art, the invention has the beneficial effects as follows: the present invention utilize extractant to the dissolubility of oxime by oxime from Oxime aqueous solution is extracted in oil phase, and is layered by oxime water separation tank, thus realize the separation of oxime water, and whole device knot Structure is simple, and separation efficiency is high, additionally it is possible to is sent back in solvent column by the mixed liquor separated, and then again separates.
Accompanying drawing explanation
Fig. 1 is present configuration schematic diagram.
In figure: 1 tank body, 2 product exit, 3 first baffle plates, 4 pure water inlets, 5 second baffles, 6 mixture exports, 7 the 3rd Baffle plate, 8 connecting tubes, 9 water pumps, 10 oxime water inlet pipes, 11 drawing liquid water pumps, 12 solvent column tower bodies, 13 agitating devices, 14 raw materials enter Mouth, 15 liquidometers.
Detailed description of the invention
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 Describe, it is clear that described embodiment is only a part of embodiment of the present invention rather than whole embodiments wholely.Based on Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under not making creative work premise Embodiment, broadly falls into the scope of protection of the invention.
Referring to Fig. 1, the present invention provides a kind of technical scheme: for the oxime water separation tank of diacetylmonoxime production, including tank body 1, solvent column tower body 12 and be arranged on the drawing liquid water pump 11 of solvent column tower body 12 intracavity bottom, the end on the right side of the inner chamber of described tank body 1 Portion is provided with product exit 2, the intracavity bottom right-to-left of described tank body 1 respectively be provided with the first vertical baffle plate 3, second Baffle plate 5 and third gear plate 7, the left side of described first baffle plate 3 is provided with pure water inlet 4, described second baffle 5 and third gear plate 7 Left side be provided with mixture export 6, described pure water inlet 4 and mixture export 6 are arranged at the intracavity bottom of tank body 1, Described mixture export 6 connects connecting tube 8, and the other end of described connecting tube 8 is connected to the right side of water pump 9, described water pump 9 Left side outfan is connected to the inner chamber left bottom of solvent column tower body 12 by pipeline, and the inner chamber of described solvent column tower body 12 is arranged Agitating device 13, the inner chamber right hand top of described solvent column tower body 12 is had to be provided with material inlet 14, the top, left side of described tank body 1 Portion is provided with liquidometer 15, and the inner chamber left bottom of described tank body 1 connects oxime water inlet pipe 10, described oxime water inlet pipe 10 The other end passes the bottom of solvent column tower body 12 and is connected on the bottom outfan of drawing liquid water pump 11.
Wherein, the half of a length of second baffle 5 of described first baffle plate 3, a length of third gear of described second baffle 5 The half of plate 7, in order to preferably separate oxime water, described first baffle plate 3, second baffle 5 and third gear plate 7 are for being set in qually spaced in The intracavity bottom of tank body 1, is provided with valve in described product exit 2, pure water inlet 4 and mixture export 6, in order to control liquid The uninterrupted that body is released, described agitating device 13 is impeller, and impeller welds with impeller axle, and impeller axle is arranged on solvent column tower Before and after body 12 on inwall, the oxime water in solvent column tower body 12 is made to be fully contacted with extractant.
Operation principle: during work, first oxime water and extractant enter in solvent column tower body 12, then by material inlet 14 It is sufficiently stirred for by the agitating device 13 in solvent column tower body 12 again, and mix homogeneously, then taking out bottom solvent column tower body 12 Oxime water containing extractant is sent in oxime water inlet pipe 10 by liquid water pump 11, during then oxime water enters the inner chamber of tank body 1, because extraction Take agent can be extracted in oil phase from oxime aqueous solution by oxime, so oxime aqueous solution can divide in the leftward space of third gear plate 7 Layer, the oil phase containing oxime is on upper strata, and aqueous phase is in lower floor, the aqueous phase mixing so the oil phase containing oxime can cross the 3rd dividing plate 7, containing oxime Liquid is flowed out by mixture export 6, and then the oil phase containing oxime is assembled, by last step in the leftward space of second baffle 5 May not separate the clean oil phase containing oxime to be further layered, the oil phase containing oxime can cross second baffle 5, and containing oxime Aqueous phase mixed liquor flows out from mixture export 6, and the purest can be in the leftward space of the first baffle plate 3 containing oxime oil phase Assemble, and the oil phase containing oxime the purest in last step is further layered, pure can cross the containing oxime oil phase One baffle plate 3, and flow out from product exit 2, the aqueous phase after three times separate is pure, and pure aqueous phase can be from only Flowing out in water out 4, during this, connecting tube 8 sends into water pump 9 by flow out in mixture export 6 containing oxime aqueous phase mixed liquor In, and by water pump 9 pressure-raising in solvent column tower body 12 sent into by pipeline.
Although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, permissible Understand and these embodiments can be carried out multiple change without departing from the principles and spirit of the present invention, revise, replace And modification, the scope of the present invention be defined by the appended.

Claims (5)

1. the oxime water separation tank produced for diacetylmonoxime, including tank body (1), solvent column tower body (12) be arranged on solvent column tower body (12) the drawing liquid water pump (11) of intracavity bottom, it is characterised in that: the inner chamber bottom right side of described tank body (1) is provided with product exit (2), the intracavity bottom right-to-left of described tank body (1) is respectively arranged with vertical the first baffle plate (3), second baffle (5) and Three baffle plates (7), the left side of described first baffle plate (3) is provided with pure water inlet (4), described second baffle (5) and third gear plate (7) Left side be provided with mixture export (6), described pure water inlet (4) and mixture export (6) and be arranged at the interior of tank body (1) Bottom chamber, described mixture export (6) connects has connecting tube (8), the other end of described connecting tube (8) to be connected to water pump (9) Right side, the left side outfan of described water pump (9) is connected to the inner chamber left bottom of solvent column tower body (12) by pipeline, described molten The inner chamber of agent tower tower body (12) is provided with agitating device (13), and the inner chamber right hand top of described solvent column tower body (12) is provided with former Material import (14), the left side top of described tank body (1) is provided with liquidometer (15), and the inner chamber left bottom of described tank body (1) is even Being connected to oxime water inlet pipe (10), the other end of described oxime water inlet pipe (10) passes the bottom of solvent column tower body (12) and is connected to On the bottom outfan of drawing liquid water pump (11).
The oxime water separation tank produced for diacetylmonoxime the most according to claim 1, it is characterised in that: described first baffle plate (3) half of a length of second baffle (5), the half of a length of third gear plate (7) of described second baffle (5).
The oxime water separation tank produced for diacetylmonoxime the most according to claim 1, it is characterised in that: described first baffle plate (3), second baffle (5) and third gear plate (7) are the intracavity bottom being set in qually spaced in tank body (1).
The oxime water separation tank produced for diacetylmonoxime the most according to claim 1, it is characterised in that: described product exit (2), it is provided with valve in pure water inlet (4) and mixture export (6).
The oxime water separation tank produced for diacetylmonoxime the most according to claim 1, it is characterised in that: described agitating device (13) being impeller, and impeller welds with impeller axle, impeller axle is arranged on before and after solvent column tower body (12) on inwall.
CN201610639709.5A 2016-08-05 2016-08-05 The oxime water separation tank produced for diacetylmonoxime Pending CN106237656A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610639709.5A CN106237656A (en) 2016-08-05 2016-08-05 The oxime water separation tank produced for diacetylmonoxime

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610639709.5A CN106237656A (en) 2016-08-05 2016-08-05 The oxime water separation tank produced for diacetylmonoxime

Publications (1)

Publication Number Publication Date
CN106237656A true CN106237656A (en) 2016-12-21

Family

ID=58078011

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610639709.5A Pending CN106237656A (en) 2016-08-05 2016-08-05 The oxime water separation tank produced for diacetylmonoxime

Country Status (1)

Country Link
CN (1) CN106237656A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111871005A (en) * 2020-07-14 2020-11-03 国家能源集团煤焦化有限责任公司 Separation device for sulfolane and heat conduction oil

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111871005A (en) * 2020-07-14 2020-11-03 国家能源集团煤焦化有限责任公司 Separation device for sulfolane and heat conduction oil
CN111871005B (en) * 2020-07-14 2022-03-01 国家能源集团煤焦化有限责任公司 Separation device for sulfolane and heat conduction oil

Similar Documents

Publication Publication Date Title
CN105727590A (en) Tubular continuous liquid-liquid extraction device and operation method thereof
CN105935578B (en) A kind of portable chemical tank with agitating function
CN209438113U (en) Pipeline mixing device is used in a kind of extraction
CN204768713U (en) Make things convenient for solid -liquid separation's reation kettle
CN205850310U (en) The oxime water separation tank that a kind of diacetylmonoxime produces
CN106237656A (en) The oxime water separation tank produced for diacetylmonoxime
CN206970508U (en) The extraction element of taxol in a kind of Chinese yew
CN203663502U (en) Oil and water two-phase liquid separation system
CN205886484U (en) Be used for pyraclostrobin production to use gas -liquid separation
CN103961900B (en) A kind of liquid-liquid extraction processing means
CN205815703U (en) A kind of reactor liquid premixing structure
CN105275445B (en) Concentric pipe type foam generator
CN205634990U (en) Hexavalent chromium ion system among anion exchange resin processing electroplating effluent
CN103803503A (en) Hydrogen peroxide extraction process with side column
CN203043864U (en) Multipurpose water-chemical mixing system
CN210303550U (en) Intelligent blending system for ethanol for cannabinoid extraction
CN104190211A (en) Device and method for increasing absorption rate of iodine-containing tail gas
Duan et al. A novel micro pipeline system for continuous extraction and recovery of phenol from aqueous solution
CN103322227A (en) Large-flow water treatment device
CN206980488U (en) A kind of solid reagent dissolving filling apparatus
CN205252930U (en) Micronize tubular blender
CN205527863U (en) Reaction unit of high -efficient greasy dirt separation
CN205007695U (en) Circulation stirring formula waste water purification device
CN204637656U (en) A kind of Horizontal oil-water separator
CN204058040U (en) High efficient mixed desanding device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20161221