CN207126152U - The carbon disulfide rectifying column of condenser built in a kind of tower top band - Google Patents

The carbon disulfide rectifying column of condenser built in a kind of tower top band Download PDF

Info

Publication number
CN207126152U
CN207126152U CN201720877977.0U CN201720877977U CN207126152U CN 207126152 U CN207126152 U CN 207126152U CN 201720877977 U CN201720877977 U CN 201720877977U CN 207126152 U CN207126152 U CN 207126152U
Authority
CN
China
Prior art keywords
condenser
tower
rectifying column
built
finished product
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
CN201720877977.0U
Other languages
Chinese (zh)
Inventor
张之峰
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.)
Shandong Xinglu Chemical Industry Ltd By Share Ltd
Original Assignee
Shandong Xinglu Chemical Industry Ltd By Share 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 Shandong Xinglu Chemical Industry Ltd By Share Ltd filed Critical Shandong Xinglu Chemical Industry Ltd By Share Ltd
Priority to CN201720877977.0U priority Critical patent/CN207126152U/en
Application granted granted Critical
Publication of CN207126152U publication Critical patent/CN207126152U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

The utility model discloses a kind of carbon disulfide rectifying column of condenser built in tower top band, including rectifying column main body, finished product delivery pipe, condenser pipe, downspout, sulphur separator and tower bottom of rectifying tower, the rectifying column body surfaces are provided with finished product extraction mouth, and finished product delivery pipe is installed on the left of finished product extraction mouth, built-in condenser is installed below the finished product delivery pipe, and condenser pipe is installed inside built-in condenser, liquid shield is installed below the condenser pipe, and downspout is installed below liquid shield, feed(raw material)inlet is installed below the downspout, and tower bottom of rectifying tower is installed below feed(raw material)inlet, waste liquid delivery pipe is installed on the left of the tower bottom of rectifying tower, and sulphur separator is installed on the left of waste liquid delivery pipe, desulphurization device is installed on the left of the sulphur separator, and sulphur pond is installed on the left of desulphurization device.Condenser avoiding device built in the utility model use damages, and reboiler utilizes bottom product liquid, improves production efficiency and reduces waste.

Description

The carbon disulfide rectifying column of condenser built in a kind of tower top band
Technical field
It the utility model is related to carbon disulfide rectifying column technical field, more particularly to two of condenser built in a kind of tower top band Nitric sulfid rectifying column.
Background technology
In fine chemistry industry production, rectifying is made extensively by people always as the main method that mutually soluble liquids mixture separates In, and rectifying column is typically widely used in the separation of liquid in chemical plant, added because its use principle is simple and bulky The various Chemical Physics reactions such as heat, reaction, and it is typically careful on carbon disulfide rectifying column, what traditional rectifying column used It is separated type external condenser, easy to use and easy realization, but exactly it is not suitable for carbon disulfide rectifying, due to distillation process In it is caused vulcanization liquefaction of hydrogen after there is severe corrosive, device is easily damaged, so being had to during carbon disulphide production Pay attention to its severe corrosive.
Utility model content
The purpose of this utility model is in order to solve shortcoming present in prior art, and built in a kind of tower top band proposed The carbon disulfide rectifying column of condenser.
To achieve these goals, the utility model employs following technical scheme:
The carbon disulfide rectifying column of condenser built in a kind of tower top band, including rectifying column main body, finished product delivery pipe, condensation Pipe, downspout, sulphur separator and tower bottom of rectifying tower, the rectifying column body surfaces are provided with finished product extraction mouth, and finished product carries Take and finished product delivery pipe is installed on the left of mouth, built-in condenser is installed below the finished product delivery pipe, and inside built-in condenser Condenser pipe is installed, liquid shield is installed, and downspout, the descending liquid are installed below liquid shield below the condenser pipe Feed(raw material)inlet is installed below pipe, and tower bottom of rectifying tower is installed below feed(raw material)inlet, is provided with the left of the tower bottom of rectifying tower Waste liquid delivery pipe, and sulphur separator is installed on the left of waste liquid delivery pipe, desulphurization device is installed on the left of the sulphur separator, and Sulphur pond is installed on the left of desulphurization device.
Preferably, reboiler is installed on the right side of the tower bottom of rectifying tower.
Preferably, vaporization escape pipe is installed above the reboiler.
Preferably, U-shaped heating tube, and installation having heaters on the right side of U-shaped heating tube are installed inside the reboiler.
Preferably, bottom product delivery pipe is installed below the U-shaped heating tube.
In the utility model, condensation is realized in rectifying column by using built-in condenser, passes through condensation Liquefaction hydrogen sulfide is still stayed in rectifying column, can reduce infringement of the severe corrosive sulfureted hydrogen liquid to device, and by using Product liquid in tower reactor is collected and vaporized and is conveyed into again in rectifying column by reboiler again, can be by liquefaction hydrogen sulfide and liquefaction two Nitric sulfid recycles again, improves the production efficiency of rectifying, reduces and wastes, and using vulcanization separator and desulphurization device be in order to By in rectifying column due to vaporization hydrogen sulfide and liquefaction carbon disulfide reaction and caused sulfur residue extract and clear up in time, can improve The operating efficiency of reboiler and tower reactor will not be blocked because of residue.
Brief description of the drawings
Fig. 1 be the utility model proposes a kind of tower top band built in condenser carbon disulfide rectifying column structural representation Figure;
Fig. 2 be the utility model proposes a kind of tower top band built in condenser carbon disulfide rectifying column reboiler knot Structure schematic diagram.
In figure:1 rectifying column main body, 2 finished product delivery pipes, 3 finished products extraction mouth, condensing unit, 5 condenser pipes, 6 liquid built in 4 Baffle plate, 7 downspouts, 8 feed(raw material)inlets, 9 waste liquid delivery pipes, 10 sulphur ponds, 11 desulphurization devices, 12 sulphur separators, 13 rectifying towers Kettle, 14 reboilers, 15 heaters, 16 bottom product delivery pipes, 17 vaporization escape pipes, 18U type heating tubes.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole Embodiment.
Reference picture 1-2, the carbon disulfide rectifying column of condenser built in a kind of tower top band, including rectifying column main body 1, finished product are defeated Pipe 2, condenser pipe 5, downspout 7, sulphur separator 12 and tower bottom of rectifying tower 13 are sent, the surface of rectifying column main body 1 is provided with finished product and carried Mouth 3 is taken, and the left side of finished product extraction mouth 3 is provided with finished product delivery pipe 2, the lower section of finished product delivery pipe 2 is provided with built-in condenser 4, and Condenser pipe 5 is installed, the lower section of condenser pipe 5 is provided with liquid shield 6, and the lower section of liquid shield 6 is provided with inside built-in condenser 4 Downspout 7, the lower section of downspout 7 is provided with feed(raw material)inlet 8, and the lower section of feed(raw material)inlet 8 is provided with tower bottom of rectifying tower 13, rectifying tower The left side of kettle 13 is provided with waste liquid delivery pipe 9, and the left side of waste liquid delivery pipe 9 is provided with sulphur separator 12, and sulphur separator 12 is left Side is provided with desulphurization device 11, and the left side of desulphurization device 11 is provided with sulphur pond 10, and the right side of tower bottom of rectifying tower 13 is provided with reboiler 14, The top of reboiler 14 is provided with vaporization escape pipe 17, U-shaped heating tube 18 is provided with inside reboiler 14, and U-shaped heating tube 18 is right Having heaters 15 is installed in side, and the U-shaped lower section of heating tube 18 is provided with bottom product delivery pipe 16.
Operation principle:When using the rectifying column, the raw material carbon disulfide after preheating is first added into feed(raw material)inlet 8, passed through Rectifying column isolate vaporization hydrogen sulfide meet built in condensing unit 4 liquefy, partial vulcanization hydrogen by condenser pipe 5 enter finished product it is defeated Pipe 2 is sent to be extracted from finished product extraction mouth 3, liquefaction hydrogen sulfide enters downspout 7 by liquid shield 6 and flows into tower bottom of rectifying tower 13 In, reboiler is entered by bottom product delivery pipe 14 with the also unreacted liquid carbon disulphide in part, these product liquid In 14, the U-shaped heating of heating tube 18 makes vaporizing liquid and is again introduced into circular response in rectifying column from vaporization escape pipe 17, and reacts Caused sulfur residue stays in tower reactor bottom and extracted by sulphur separator 12, enters by desulphurization device 11 in sulphur pond 10.
It is described above, the only preferable embodiment of the utility model, but the scope of protection of the utility model is not This is confined to, any one skilled in the art is in the technical scope that the utility model discloses, according to this practicality New technical scheme and its utility model design are subject to equivalent substitution or change, should all cover in protection model of the present utility model Within enclosing.

Claims (5)

1. the carbon disulfide rectifying column of condenser built in a kind of tower top band, including rectifying column main body(1), finished product delivery pipe(2), it is cold Solidifying pipe(5), downspout(7), sulphur separator(12)And tower bottom of rectifying tower(13), it is characterised in that the rectifying column main body(1) Surface is provided with finished product extraction mouth(3), and finished product extraction mouth(3)Left side is provided with finished product delivery pipe(2),
The finished product delivery pipe(2)Lower section is provided with built-in condenser(4), and built-in condenser(4)Inside is provided with condenser pipe (5), the condenser pipe(5)Lower section is provided with liquid shield(6), and liquid shield(6)Lower section is provided with downspout(7), it is described Downspout(7)Lower section is provided with feed(raw material)inlet(8), and feed(raw material)inlet(8)Lower section is provided with tower bottom of rectifying tower(13), the rectifying Tower tower reactor(13)Left side is provided with waste liquid delivery pipe(9), and waste liquid delivery pipe(9)Left side is provided with sulphur separator(12), institute State sulphur separator(12)Left side is provided with desulphurization device(11), and desulphurization device(11)Left side is provided with sulphur pond(10).
2. the carbon disulfide rectifying column of condenser built in a kind of tower top band according to claim 1, it is characterised in that institute State tower bottom of rectifying tower(13)Right side is provided with reboiler(14).
3. the carbon disulfide rectifying column of condenser built in a kind of tower top band according to claim 2, it is characterised in that institute State reboiler(14)Top is provided with vaporization escape pipe(17).
4. the carbon disulfide rectifying column of condenser built in a kind of tower top band according to claim 2, it is characterised in that described Reboiler(14)Inside is provided with U type heating tubes(18), and U type heating tubes(18)Right side is installed by having heaters(15).
5. the carbon disulfide rectifying column of condenser built in a kind of tower top band according to claim 4, it is characterised in that described U-shaped heating tube(18)Lower section is provided with bottom product delivery pipe(16).
CN201720877977.0U 2017-07-19 2017-07-19 The carbon disulfide rectifying column of condenser built in a kind of tower top band Active CN207126152U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720877977.0U CN207126152U (en) 2017-07-19 2017-07-19 The carbon disulfide rectifying column of condenser built in a kind of tower top band

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720877977.0U CN207126152U (en) 2017-07-19 2017-07-19 The carbon disulfide rectifying column of condenser built in a kind of tower top band

Publications (1)

Publication Number Publication Date
CN207126152U true CN207126152U (en) 2018-03-23

Family

ID=61639178

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720877977.0U Active CN207126152U (en) 2017-07-19 2017-07-19 The carbon disulfide rectifying column of condenser built in a kind of tower top band

Country Status (1)

Country Link
CN (1) CN207126152U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107213663A (en) * 2017-07-19 2017-09-29 成都尚智恒达科技有限公司 The carbon disulfide rectifying column of condenser built in a kind of tower top band

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107213663A (en) * 2017-07-19 2017-09-29 成都尚智恒达科技有限公司 The carbon disulfide rectifying column of condenser built in a kind of tower top band

Similar Documents

Publication Publication Date Title
CN105967425A (en) Coal chemical industry grey water flashing treatment system capable of reducing ammonia accumulation and coal chemical industry grey water flashing treatment process capable of reducing ammonia accumulation
CN102241453A (en) Method for treating coal gasification wastewater containing phenol and ammonia
CN207126152U (en) The carbon disulfide rectifying column of condenser built in a kind of tower top band
CN201855641U (en) Device for treating tail gas containing hydrogen chloride
CN206126864U (en) It prepares device of pure liquid ammonia to contain ammonia transform lime set waste water
CN107213663A (en) The carbon disulfide rectifying column of condenser built in a kind of tower top band
CN104262376A (en) TMSOTf (trimethylsilyl trifluoromethanesulfonate) purifying method
CN204897395U (en) Purifier of chlorinated paraffin by -product hydrogen chloride
CN103157292A (en) Clean dewatering device for toluenediamine
CN115560541A (en) Hydrocone type refrigerated krypton-xenon refining device
CN214299720U (en) Phenol sodium salt decomposes effluent treatment plant
CN105110350B (en) Ammonia recovery system and ammonia recovery method
CN115060042A (en) Hydrocone type refrigerated krypton-xenon refining device
CN105217654B (en) Alkylation waste sulfuric acid recycling treatment device and method
CN208038351U (en) A kind of device of continuous production methyl mercaptan salting liquid
CN211035309U (en) Novel phenol ammonia recovery device for efficiently recovering ammonia
CN110791327B (en) Device and process for deeply removing purified gas sulfide of low-temperature methanol washing system
CN210434014U (en) Novel trinity rectifying column apparatus for producing of industry hydrogen peroxide solution enrichment facility
CN207877294U (en) A kind of recycling system for preparing ortho-aminotoluene and generating waste water
CN107141199A (en) Methanol mother liquor is without refluxed cryogenic rectificating method and equipment
CN207429733U (en) A kind of rectifying device for being used to prepare watermelon ketone
CN206955650U (en) A kind of purification system of fume colloidal silica production silicon tetrachloride
CN105693000A (en) Recovery processing technology for phloroglucinol production wastewater
CN106395858B (en) A kind of method and device converting lime set waste water making pure liquefied ammonia containing ammonia
CN106629936A (en) Technology and system used for processing waste water

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant