CN207169074U - A kind of ethanol distillation device of nitrocotton - Google Patents

A kind of ethanol distillation device of nitrocotton Download PDF

Info

Publication number
CN207169074U
CN207169074U CN201721053459.3U CN201721053459U CN207169074U CN 207169074 U CN207169074 U CN 207169074U CN 201721053459 U CN201721053459 U CN 201721053459U CN 207169074 U CN207169074 U CN 207169074U
Authority
CN
China
Prior art keywords
destilling tower
ethanol
return tank
pans
nitrocotton
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.)
Active
Application number
CN201721053459.3U
Other languages
Chinese (zh)
Inventor
徐赟
蒋保军
宗建山
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.)
Nantong Tailida Chemical Co Ltd
Original Assignee
Nantong Tailida Chemical 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 Nantong Tailida Chemical Co Ltd filed Critical Nantong Tailida Chemical Co Ltd
Priority to CN201721053459.3U priority Critical patent/CN207169074U/en
Application granted granted Critical
Publication of CN207169074U publication Critical patent/CN207169074U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

It the utility model is related to alcohol distillation technical field, specifically disclose a kind of ethanol distillation device of nitrocotton, including raw material pans, destilling tower, return tank and finished product pans, raw material pans are connected with destilling tower, the tower top of destilling tower is provided with overhead condenser, the connection with return tank of overhead condenser, return tank are connected with destilling tower and finished product pans respectively.The utility model device is effectively distilled by destilling tower to ethanol, the potential safety hazard easily exploded when eliminating distillation, there is provided return tank, partial reflux after increase ethanol distillation, the liquid-phase reflux of tower top can ensure the progress of still-process continuous-stable, increase the efficiency and ethanol collection rate of ethanol distillation.

Description

A kind of ethanol distillation device of nitrocotton
Technical field
The utility model belongs to alcohol distillation technical field, and in particular to a kind of ethanol distillation device of nitrocotton.
Background technology
Ethanol is largely applied in industry-by-industry as a kind of basic industrial raw material.3000t/a coating nitre Change cotton (containing alcohol=25%, nitrogenous=12.6%) for product in rear road ethanol expelling water process, caused 65% Diluted Alcohol is usual Distilation is needed to recycle, at present, for the distillation technique of ethanol, its principle is that the boiling point of ethanol is less than the boiling of other solution Point, heating ethanol make its evaporation, turn into liquid by condensation, the purpose of recovery higher degree ethanol is reached with this.
Nitrocotton is white or slightly yellow flocculence, can be dissolved in acetone.Scientific name cellulose nitrate, be once called as nitrocellulose, Nitrocotton.NC is a polymer, and its molecular weight is very big.Its molecular formula is that C6H7O2 (ONO2) a (OH) 3-an, wherein a is Esterification degree, n are the degree of polymerization.Degree of esterification traditionally is represented with nitrogen content percentage, nitrocotton has high flammability and blast Property, for its degree of danger depending on degree of nitration, nitrocotton of the nitrogen content more than 12.5% is dangerous greatly, meets fire and fires Burn.
Conventional alcohol distillation device is that steam rod is placed directly on to directly heat inside the alcohol containing nitrocotton and makes its evaporation, Because nitrocotton belongs to combustible and explosive articles, so such distilling apparatus carries out easily causing the quick-fried of nitrocotton during alcohol distillation It is fried, great potential safety hazard be present.
Utility model content
Technical problem to be solved in the utility model is in view of the shortcomings of the prior art, there is provided a kind of ethanol of nitrocotton Distilling apparatus, the distillation of safe and environment-friendly progress nitrocotton, solve easily to cause what nitrocotton exploded during ethanol distillation Hidden danger.
In order to solve the above technical problems, a kind of ethanol distillation device of nitrocotton of the utility model, including raw material pans, Destilling tower, return tank and finished product pans, the outlet of the raw material pans are connected with destilling tower, and the tower top of the destilling tower is set There is overhead condenser, the outlet of the overhead condenser is connected with the import of the return tank, the outlet difference of the return tank It is connected with destilling tower and finished product pans.
Further, it is provided with cooler between return tank and the finished product pans.
Preferably, feedstock transportation pump is provided between the raw material pans and destilling tower.
Preferably, the bottom of the return tank is connected with reflux pump.
Further, the distillation tower bottom is connected with decontamination water treatment system.
The beneficial effects of the utility model are:The ethanol distillation device of the utility model nitrocotton, it is effective by destilling tower Ground distills to ethanol, eliminates the potential safety hazard easily exploded when being distilled using steam wand, is also provided with back Tank is flowed, increases partial reflux after ethanol distillation, the liquid-phase reflux of tower top can ensure the progress of still-process continuous-stable, increase The efficiency and ethanol collection rate of ethanol distillation, collection rate is up to more than 98%.
Brief description of the drawings
, below will be to institute in embodiment or description of the prior art in order to illustrate more clearly of the technical solution of the utility model The accompanying drawing needed to use is briefly described, it should be apparent that, drawings in the following description are only more of the present utility model Embodiment, for those of ordinary skill in the art, on the premise of not paying creative work, can also be attached according to these Figure obtains other accompanying drawings.
Fig. 1 is the structural representation of the utility model distilling apparatus.
In figure:1- raw material pans, 2- destilling towers, 3- return tanks, 4- finished product pans, 5- overhead condensers, 6- coolings Device, 7- feedstock transportation pumps, 8- reflux pumps, 9- decontamination water treatment systems.
Embodiment
The technical scheme in the embodiment of the utility model will be clearly and completely described below, it is clear that described Embodiment is only the utility model part of the embodiment, rather than whole embodiments.Based on the implementation in the utility model Example, the every other embodiment that those of ordinary skill in the art are obtained on the premise of creative work is not made, all belongs to In the scope of the utility model protection.
In a specific embodiment of the present utility model, a kind of ethanol distillation device of nitrocotton, including raw material are disclosed Pans 1, destilling tower 2, return tank 3 and finished product pans 4,
The outlet of the raw material pans 1 is connected with destilling tower 2, and original is provided between the raw material pans 1 and destilling tower 2 Material conveying pump 7, the feedstock transportation pump 7 are in normal temperature, atmospheric pressure state, and 65% ethanol solution in raw material pans 1 passes through Feedstock transportation pump 7 is pumped into destilling tower 2;
The tower top of the destilling tower 2 is provided with overhead condenser 5, and the overhead condenser 5 is in normal temperature, atmospheric pressure state, institute State the bottom of destilling tower 2 and be connected with decontamination water treatment system 9, the outlet of the overhead condenser 5 connects with the import of the return tank 3 Connect, the overhead condenser 5 can carry out cooling water circulation to destilling tower 2, be distilled with reference to the steam valve of bottom of towe, after distillation Alcohol vapour from tower top after overhead condenser cools down to return tank;Raffinate then enters decontamination water treatment system 9 from destilling tower bottom;
The outlet of the return tank 3 is connected with destilling tower 2 and finished product pans 4 respectively, the bottom connection of the return tank 3 There is reflux pump 8, the reflux pump 8 is under normal temperature, atmospheric pressure state and worked, and is provided between the return tank 3 and finished product pans 4 Cooler 6, the cooler 6 are at normal temperature, atmospheric pressure state, reflux pump 8 one of the condensate liquid through tank bottom in return tank 3 Point be delivered to destilling tower backflow, it is a part of then to the rear enclosure of finished product pans 4 use after subcooler 6.
The ethanol distillation process of the utility model nitrocotton is:65% ethanol solution from ethanol expelling water workshop section enters former After expecting pans 1, destilling tower 2 is entered by feedstock transportation pump 7, the tower top temperature of destilling tower 2 is 80 DEG C, and column bottom temperature is 105 DEG C, pressure is normal pressure, and the circulating cooling penstock opened in overhead condenser 5 carries out cooling water circulation, when in destilling tower 2 Material liquid level reach requirement after, open tower bottom steam valve distilled, alcohol vapour cools down from tower top through overhead condenser 5 Afterwards to return tank 3, raffinate then enters waste water decontamination water treatment system 9, and the temperature of return tank 3 is 30 DEG C, and pressure is normal pressure, is returned Stream, 3 inner condensat liquids are delivered to destilling tower 2 through tank bottom reflux pump 30% and flow back, 70% after the cooling of subcooler 6 among finished product The rear enclosure of tank 4 is used.
The beneficial effects of the utility model are:The ethanol distillation device of the utility model nitrocotton, it is effective by destilling tower Ground distills to ethanol, eliminates the potential safety hazard easily exploded when being distilled using steam wand, is also provided with back Tank is flowed, increases partial reflux after ethanol distillation, the liquid-phase reflux of tower top can ensure the progress of still-process continuous-stable, increase The efficiency and ethanol collection rate of ethanol distillation, collection rate is up to more than 98%.
Described above is preferred embodiment of the present utility model, it is noted that for the ordinary skill of the art For personnel, on the premise of the utility model principle is not departed from, some improvements and modifications can also be made, these are improved and profit Decorations are also considered as the scope of protection of the utility model.

Claims (5)

1. the ethanol distillation device of a kind of nitrocotton, it is characterised in that including raw material pans (1), destilling tower (2), return tank (3) it is connected with finished product pans (4), the outlet of the raw material pans (1) with destilling tower (2), the tower top of the destilling tower (2) Provided with overhead condenser (5), the outlet of the overhead condenser (5) is connected with the import of the return tank (3), the return tank (3) outlet is connected with destilling tower (2) and finished product pans (4) respectively.
A kind of 2. ethanol distillation device of nitrocotton according to claim 1, it is characterised in that the return tank (3) with Cooler (6) is provided between finished product pans (4).
A kind of 3. ethanol distillation device of nitrocotton according to claim 1, it is characterised in that the raw material pans (1) feedstock transportation pump (7) is provided between destilling tower (2).
4. the ethanol distillation device of a kind of nitrocotton according to claim 2, it is characterised in that the return tank (3) Bottom is connected with reflux pump (8).
A kind of 5. ethanol distillation device of nitrocotton according to claim 3, it is characterised in that destilling tower (2) bottom Portion is connected with decontamination water treatment system (9).
CN201721053459.3U 2017-08-22 2017-08-22 A kind of ethanol distillation device of nitrocotton Active CN207169074U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721053459.3U CN207169074U (en) 2017-08-22 2017-08-22 A kind of ethanol distillation device of nitrocotton

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721053459.3U CN207169074U (en) 2017-08-22 2017-08-22 A kind of ethanol distillation device of nitrocotton

Publications (1)

Publication Number Publication Date
CN207169074U true CN207169074U (en) 2018-04-03

Family

ID=61740422

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721053459.3U Active CN207169074U (en) 2017-08-22 2017-08-22 A kind of ethanol distillation device of nitrocotton

Country Status (1)

Country Link
CN (1) CN207169074U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107362563A (en) * 2017-08-22 2017-11-21 南通泰利达化工有限公司 The ethanol distillation technique and device of a kind of nitrocotton

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107362563A (en) * 2017-08-22 2017-11-21 南通泰利达化工有限公司 The ethanol distillation technique and device of a kind of nitrocotton

Similar Documents

Publication Publication Date Title
CN104557511B (en) A kind of method of acrylic acid from vinylformic acid sour water
CN104151136B (en) The processing method of butanols-N-BUTYL ACETATE is reclaimed from antibiotic production wastewater
CN104844456B (en) A kind of n-butyl acrylate waste oil recovery process and device
CN208493282U (en) A kind of dehydration distillation system of stripper regeneration technology section
CN207169074U (en) A kind of ethanol distillation device of nitrocotton
CN103951544B (en) Method for separating ethyl acetate and ethanol azeotrope by differential pressure rectification
CN204891261U (en) Alcohol purification recovery unit
CN107915580A (en) A kind of ethylene glycol multi-effect distillation system and process
CN107793293A (en) Method for separating methanol-isopropanol-water by intermittent extraction and rectification and control structure
CN208485823U (en) A kind of combination unit for realizing azeotropic rectifying continuous operation
CN106278882A (en) A kind of butyl acrylate production system neutralized without alkali and production method thereof
CN103772185B (en) Device and method for removing moisture and heteroacids in acetic acid
CN106431884B (en) A kind of butyraldehyde oxidation prepares the device and method of butyric acid
CN106349107B (en) A kind of method and device of heterogeneous azeotropic rectification separating acetonitrile-triethylamine mixture
CN104860819A (en) Method and system for separating butyl acetate and n-butanol through coupling of pressure-swing distillation and heat-pump distillation
CN205653372U (en) Light system takes off in propylene glycol methyl ether acetate production
CN107362563A (en) The ethanol distillation technique and device of a kind of nitrocotton
CN103706136A (en) Double-rectifying-tower series separation and purification method for recovery of methyl tert-butyl ether-tetrahydrofuran in waste liquid in statins synthesis process
CN106693429A (en) Treatment system and method for ethyl acetate production water
CN212282924U (en) THF (tetrahydrofuran) rectifying device for PBT (polybutylene terephthalate) production
CN212246831U (en) Acetic acid azeotropic dehydration device suitable for producing trimellitic anhydride
CN204644234U (en) A kind of n-butyl acrylate drain oil recovery equipment
CN106316793A (en) Alcohol preparing device and method based on the double rectification column and six-column and four-effect distillation
CN208279337U (en) A kind of methanol-to-olefins sour water stripper
CN210506156U (en) Methyl propionate, methyl alcohol, water ternary azeotrope separator

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant