CN207445653U - Sulphur ammonium crystallization recycling energy saver in acrylonitrile process - Google Patents
Sulphur ammonium crystallization recycling energy saver in acrylonitrile process Download PDFInfo
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- CN207445653U CN207445653U CN201721457284.2U CN201721457284U CN207445653U CN 207445653 U CN207445653 U CN 207445653U CN 201721457284 U CN201721457284 U CN 201721457284U CN 207445653 U CN207445653 U CN 207445653U
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- heater
- crystallizer
- tank
- outlet
- sulphur ammonium
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- 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.)
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- -1 Sulphur ammonium Chemical compound 0.000 title claims abstract description 46
- NLHHRLWOUZZQLW-UHFFFAOYSA-N acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims abstract description 21
- 238000002425 crystallisation Methods 0.000 title claims abstract description 17
- 230000005712 crystallization Effects 0.000 title claims abstract description 17
- 238000004064 recycling Methods 0.000 title claims abstract description 10
- 229920000642 polymer Polymers 0.000 claims abstract description 53
- 239000007788 liquid Substances 0.000 claims abstract description 28
- BFNBIHQBYMNNAN-UHFFFAOYSA-N Ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229910052921 ammonium sulfate Inorganic materials 0.000 claims abstract description 26
- 235000011130 ammonium sulphate Nutrition 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000002562 thickening agent Substances 0.000 claims abstract description 14
- 238000004806 packaging method and process Methods 0.000 claims abstract description 9
- 239000007787 solid Substances 0.000 claims abstract description 9
- 239000002002 slurry Substances 0.000 claims abstract description 7
- 239000012452 mother liquor Substances 0.000 claims description 25
- 239000000243 solution Substances 0.000 claims description 24
- 239000012047 saturated solution Substances 0.000 claims description 5
- 238000009434 installation Methods 0.000 abstract description 14
- 238000005516 engineering process Methods 0.000 abstract description 7
- JZRWCGZRTZMZEH-UHFFFAOYSA-N Thiamine Natural products CC1=C(CCO)SC=[N+]1CC1=CN=C(C)N=C1N JZRWCGZRTZMZEH-UHFFFAOYSA-N 0.000 abstract description 5
- 238000000926 separation method Methods 0.000 abstract description 5
- 229960003495 thiamine Drugs 0.000 abstract description 5
- 235000019157 thiamine Nutrition 0.000 abstract description 5
- 239000011721 thiamine Substances 0.000 abstract description 5
- 238000011084 recovery Methods 0.000 abstract description 4
- KYMBYSLLVAOCFI-UHFFFAOYSA-N thiamine Chemical compound CC1=C(CCO)SCN1CC1=CN=C(C)N=C1N KYMBYSLLVAOCFI-UHFFFAOYSA-N 0.000 abstract description 4
- 239000005864 Sulphur Substances 0.000 abstract description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 abstract description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract description 2
- 238000001704 evaporation Methods 0.000 description 10
- 239000007789 gas Substances 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- LELOWRISYMNNSU-UHFFFAOYSA-N Hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 description 4
- WEVYAHXRMPXWCK-UHFFFAOYSA-N acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 4
- 239000006227 byproduct Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- USDJRNOUHRLPDS-UHFFFAOYSA-N C#N.C1CO1 Chemical compound C#N.C1CO1 USDJRNOUHRLPDS-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000015450 Tilia cordata Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- KAAXBZZRAZARDL-UHFFFAOYSA-N C#N.C#C Chemical compound C#N.C#C KAAXBZZRAZARDL-UHFFFAOYSA-N 0.000 description 1
- 239000005997 Calcium carbide Substances 0.000 description 1
- UIXRSLJINYRGFQ-UHFFFAOYSA-N Calcium carbide Chemical compound [Ca+2].[C-]#[C-] UIXRSLJINYRGFQ-UHFFFAOYSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- ILTOXTLKSTUJJS-UHFFFAOYSA-N acetylene;molecular hydrogen Chemical compound [H][H].C#C ILTOXTLKSTUJJS-UHFFFAOYSA-N 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 125000003700 epoxy group Chemical group 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000011555 saturated liquid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing Effects 0.000 description 1
- 150000003544 thiamines Chemical class 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
Abstract
The utility model is mainly used in acrylonitrile installation thiamine recovery power-saving technology technique,Sulphur ammonium crystallization recycling energy saver in more particularly to a kind of acrylonitrile process,Its device is included through the sequentially connected dilute sulphur ammonium storage tank of pipeline,Preheater,Crystallizer,Heater and condensate tank,Dilute sulphur ammonium feed pump is set between dilute sulphur ammonium storage tank and preheater,Compressor is set between crystallizer top exit and heater,Crystalliser feet outlet connects thickener by slurry delivery pump,The top of the top connection crystallizer of heater,The bottom of heater connects the lower part of heater by circulating pump,Heater forms forced circulation with crystallizer by circulating pump,Condensate tank top sets gas outlet,Bottom connects acrylonitrile installation by condensate delivery pump,Thickener outlet centrifuge,Centrifuge includes liquid outlet and solid outlet,Solid outlet connects packaging kit equipment.High polymer separation is thorough in the utility model saving steam, saving recirculated water and ammonium sulfate solution.
Description
Technical field
The utility model is related to sulphur ammonium crystallization recycling energy savers in a kind of acrylonitrile process, are mainly used in acrylonitrile dress
Put thiamine recovery power-saving technology technique.
Background technology
The current main ethylene oxide-hydrogen cyanide of production method (dehydration of 3- hydroxies) method of acrylonitrile, acetylene in the world-
Three kinds of hydrogen cyanide method, propylene ammmoxidation process.Ethylene oxide-acrylonitrile purity made from hydrogen cyanide method is higher, but raw material epoxy second
Alkane is expensive, and synthesis technology is complicated, therefore after the advent of acetylene-hydrogen cyanide method, that is, is eliminated.Acetylene-hydrogen cyanide method has gas
Two kinds of phase method and liquid phase method, the latter is better than the former, and obtains commercial Application.This method is simpler than ethylene oxide-hydrogen cyanide method, cost compared with
It is low, but the raw material calcium carbide of acetylene need to consume substantial amounts of electric energy, therefore limited by electric power resource and environmental protection.Propylene, ammonia oxidation
Have many advantages, such as that raw material is easy to get, product cost is low, technical process is simple, capital expenditure saves therefore rapidly instead of other tradition sides
Method, acrylonitrile installation in the world is generally using propylene, ammonia oxidation at present.While propylene, ammonia oxidation production acrylonitrile,
By-product hydrogen cyanide, acetonitrile and sulphur ammonium.Wherein, the ammonium sulfate solution of 20% or so concentration of acrylonitrile installation upstream by-product, generally use
Evaporative crystallization technique, by-product thiamine fertilizer.The sulphur ammonium unit of acrylonitrile installation produces sulphur using single effect evaporation crystallization technique earliest
Ammonium fertilizer.Two-effect evaporation crystallization technique was developed to later, two-effect evaporation crystallization technique is than single effect evaporation crystallization technique energy consumption significantly
It reduces.But steam is needed to consume a large amount of steam as heat source.Operating cost is still high, energy-saving effect unobvious.
Utility model content
The technical problems to be solved in the utility model is：There is provided a kind of operating cost significantly reduces, and energy saving aspect has great
It breaks through, meanwhile, the high polymer isolated from sulphur ammonium liquid does not carry sulphur ammonium so that acrylonitrile installation waster water incinerator is burning height
It is more environmentally-friendly during polymers, sulphur ammonium crystallization recycling energy saver in the acrylonitrile process of more preferable environmental protection.
Sulphur ammonium crystallization recycling energy saver in acrylonitrile process described in the utility model, including being sequentially connected by pipeline
Dilute sulphur ammonium storage tank, preheater, crystallizer, heater and condensate tank, set between dilute sulphur ammonium storage tank and preheater dilute sulphur ammonium into
Material pump, sets compressor between crystallizer top exit and heater, crystalliser feet outlet is connected thick by slurry delivery pump
Thick device, the top of the top connection crystallizer of heater, the bottom of heater connect the lower part of heater by circulating pump, heating
Device forms forced circulation with crystallizer by circulating pump, and condensate tank top sets gas outlet, and bottom is connected by condensate delivery pump
Acrylonitrile installation, thickener outlet centrifuge, centrifuge include liquid outlet and solid outlet, and solid outlet connection is complete
Packaging facilities.
Dilute sulphur ammonium comes from acrylonitrile installation.
Overflow port, overflow port connection mother liquor tank, the liquid outlet connection mother liquor of centrifuge are set at the top of the thickener
Tank, mother liquor tank connect the bottom of heater by saturated solution feed pump.
Polymer exit is set in the middle part of the crystallizer, and polymer exit connects polymer by saturation liquid pump and separates
Tank, polymer separation tank bottom portion set polymer exit and ammonium sulfate solution to export respectively, polymer exit connection polymer buffer
Tank, polymer buffer pot bottom by polymer delivery pump connect waster water incinerator, ammonium sulfate solution outlet mother liquor surge tank,
Mother liquor surge tank pumps the bottom of connection heater by mother liquor.
There is special structure in the middle part of crystallizer --- " armpit structure ", the organic matters such as polymer can be assembled since proportion is small
At " armpit structure ", 6 interfaces are uniformly opened in 360 ° of a circle scopes, 6 interfaces extract the organic matters such as polymer out, and carry
Substantial amounts of sulphur ammonium liquid.It takes over to converge for 6 and is pumped to polymer knockout drum for a pipeline desaturation liquid, polymer knockout drum uses
House journal " high-efficiency layered separator of acrylonitrile unit " technology, can thoroughly separate polymer and sulphur ammonium liquid, prevent sulphur ammonium
Liquid removes incinerator, reduces the discharge of sulfide.
Diluted thioamine liquid is preheated by preheater, and the solution after preheating is sent in crystallizer.It is at the initial stage of driving, it is necessary to outer
Portion provides middle pressure steam as heat source.Middle pressure steam removes heater, heats ammonium sulfate solution, and the water vapour of vaporization is from crystallizer top row
Go out, water vapour its pressure, temperature after compressor compresses have rise, and compressed steam is dense as the heat source heating of heater
Contracting sulphur ammonium liquid.Steam is condensed in the heater, and lime set goes acrylonitrile installation reuse as chilled water (chw)；Solution pumps in crystallizer
Forced circulation is returned in crystallizer after heated device, ammonium sulfate in heater with compressed steam heat-exchanging, required for acquisition
Heat achieve the purpose that evaporation and concentration, while steam is condensed.It is heat source that middle pressure steam is not required during normal production, therefore can
To save steam and recirculated water.
A small amount of polymer in sulphur ammonium liquid, micro acrylonitrile, acetonitrile and hydrogen cyanide are assembled at the top of crystallizer outer layer,
And it separates.The polymer solution isolated still containing part ammonium sulfate solution, is sent to the separation of polymer knockout drum, polymerization
Object adds in a certain amount of chilled water (chw) (from sulphur ammonium liquid from the overflow of separator top to polymer buffer tank in polymer buffer tank
In the water that steams) send to burning after dilution；The ammonium sulfate solution isolated from separator bottom, which is sent back in heater, continues evaporation knot
It is brilliant；
After sulphur ammonium liquid after concentrate is transported to thickener continuation enrichment, product solid ammonium sulfate is obtained through centrifuge dewatering
Grain；Ammonium sulfate products are sent after being sent into packaging kit machine packaging to warehouse.
The beneficial effects of the utility model are：
1st, steam is saved：A small amount of steam only is needed when sulphur ammonium unit is driven, as unit starting heat source.During normal production
Need only to external a small amount of steam.During normal production, the steam of ammonium sulfate solution evaporation is by compressor compresses, to improve steam
Pressure and temperature improves the steam of pressure and temperature as heat source, to evaporate ammonium sulfate solution.
2nd, recirculated water is saved：Common thiamine recovery technology is, it is necessary to cycle using single-action or two-effect evaporation crystallization technique
Water is as low-temperature receiver, to condense the steam evaporated from sulphur ammonium liquid.This technique the steam evaporated in sulphur ammonium liquid through overcompression,
Its temperature and pressure is improved, and heat source is used as to evaporate ammonium sulfate solution, itself becomes condensate liquid, is not required recirculated water cold
It is solidifying.
3rd, high polymer separation is thorough in ammonium sulfate solution：In the ammonium sulfate solution of 20% or so concentration of acrylonitrile installation upstream by-product
There is a small amount of high polymer, these high polymers needs are separated.The benefit separated is：First, sulphur ammonium quality is improved；
Second is that the waster water incinerator of acrylonitrile installation can be removed as fuel, it can be energy saving.Pervious high polymer separation is always not thorough,
Some ammonium sulfate solutions are carried, so when burning high polymer, the sulphur ammonium of carrying is burned together, sulfur dioxide (SO2) is generated, to cigarette
The processing of gas makes troubles.This thiamine recovery power-saving technology can be completely separated the high polymer in ammonium sulfate solution (including acrylonitrile
Wait organic matters).
Description of the drawings
Fig. 1 is the structure diagram of the utility model.
In figure：1st, preheater；2nd, crystallizer；3rd, compressor；4th, circulating pump；5th, heater；6th, condensate tank；7th, polymer point
From tank；8th, polymer buffer tank；9th, thickener；10th, centrifuge；11st, mother liquor tank；12nd, packaging kit equipment；13rd, waste water incineration
Stove；14th, saturated solution feed pump；15th, polymer delivery pump；16th, mother liquor surge tank；17th, mother liquor pumps；18th, condensate delivery pump；
19th, saturation liquid pump；20th, slurry delivery pump；21st, acrylonitrile installation；22nd, dilute sulphur ammonium feed pump；23rd, dilute sulphur ammonium storage tank.
Specific embodiment
The utility model is described further below in conjunction with the accompanying drawings：
As shown in Figure 1, sulphur ammonium crystallization recycling energy saver in acrylonitrile process described in the utility model, including passing through pipe
The sequentially connected dilute sulphur ammonium storage tank 23 in road, preheater 1, crystallizer 2, heater 5 and condensate tank 6, dilute sulphur ammonium storage tank 23 and preheating
Dilute sulphur ammonium feed pump 22 between device 1 is set, compressor 3,2 bottom of crystallizer are set between 2 top exit of crystallizer and heater 5
Outlet connects thickener 9, the top of the top connection crystallizer 2 of heater 5, the bottom of heater 5 by slurry delivery pump 20
The lower part of heater 5 is connected by circulating pump 4, heater 5 forms forced circulation, condensate tank 6 with crystallizer 2 by circulating pump 4
Top set gas outlet, bottom by condensate delivery pump 18 connect acrylonitrile installation 21,9 outlet centrifuge 10 of thickener,
Centrifuge 10 includes liquid outlet and solid outlet, solid outlet connection packaging kit equipment 12.9 top of thickener sets overflow
Mouthful, overflow port connection mother liquor tank 11, the liquid outlet of centrifuge 10 connects mother liquor tank 11, and mother liquor tank 11 passes through saturated solution feed pump
The bottom of 14 connection heaters 5.2 middle part of crystallizer sets polymer exit, and polymer exit is connected poly- by saturation liquid pump 19
Object knockout drum 7 is closed, 7 bottom of polymer knockout drum sets polymer exit and ammonium sulfate solution to export respectively, polymer exit connection
Polymer buffer tank 8,8 bottom of polymer buffer tank connect waster water incinerator 13 by polymer delivery pump 15, and ammonium sulfate solution goes out
Mouth connection mother liquor surge tank 16, mother liquor surge tank 16 pass through the bottoms of 17 connection heaters 5 of mother liquor pump.
Processing step is as follows：
1) from extraneous next diluted thioamine liquid into dilute sulphur ammonium storage tank 23, sent through dilute sulphur ammonium feed pump 22 into preheater 1 in advance
Heat is to 104 DEG C；
2) ammonium sulfate solution after preheating enters crystallizer 2,2 basidixed of crystallizer into steam, after 3 Pressurized-heated of compressor
Supply heater 5 as heat source, the lime set of heater 5 is sent to condensate tank 6,6 gas phase of condensate tank after emptying condenser condensation not
Solidifying gas removes washer of dropping a hint, condensate liquid sent through condensate delivery pump 18 to 21 reuse of acrylonitrile installation or as flushing water send to
Each user is rinsed；
3) ammonium sulfate solution is cycled through circulating pump semi-finals system, and ammonium sulfate solution is sent into after heater 5 heats and returns to crystallizer 2, is tying
The vapor of vaporization is isolated in brilliant device 2, generation steam removes compressor 3, utilized after being compressed as heat source；
4) after 2 bottom slurry of crystallizer is sent into 9 crystallisation by cooling of thickener by slurry delivery pump 20, centrifuge 10 is flowed into certainly,
Through being centrifuged at a high speed, isolate solid ammonium sulfate and go packaging kit equipment 12, packed sulphur ammonium is obtained after packaging kit equipment 12
Product.
The mother liquor that the mother liquor and centrifuge 10 that 9 top overflow of thickener goes out in step 4) are isolated flows into mother liquor tank 11 certainly,
Re-evaporation in heater 5 is returned with saturated solution feed pump 14 to crystallize.
2 middle part extraction polymer of crystallizer, and sulphur ammonium liquid is carried, sulphur ammonium liquid is saturated liquid pump 19 and send to polymer knockout drum
7, the polymer isolated removes polymer buffer tank 8, and waste water incineration is sent to through polymer delivery pump 15 after stirring；Polymer separates
The ammonium sulfate solution isolated in tank 7 enters mother liquor surge tank 16, and being transported to heater 5 through mother liquor pump 17 continues evaporation knot
It is brilliant.
Claims (3)
1. a kind of sulphur ammonium crystallization recycling energy saver in acrylonitrile process, it is characterised in that：Including sequentially connected by pipeline
Dilute sulphur ammonium storage tank (23), preheater (1), crystallizer (2), heater (5) and condensate tank (6), dilute sulphur ammonium storage tank (23) and preheating
Dilute sulphur ammonium feed pump (22) between device (1) is set, compressor (3) is set between crystallizer (2) top exit and heater (5),
Crystallizer (2) outlet at bottom connects thickener (9), the top connection crystallizer (2) of heater (5) by slurry delivery pump (20)
Top, the bottom of heater (5) connects the lower part of heater (5) by circulating pump (4), and heater (5) is logical with crystallizer (2)
It crosses circulating pump (4) and forms forced circulation, gas outlet is set at the top of condensate tank (6), and bottom connects third by condensate delivery pump (18)
Alkene nitrile device (21), thickener (9) outlet centrifuge (10), centrifuge (10) include liquid outlet and solid outlet, Gu
Body outlet packaging kit equipment (12).
2. sulphur ammonium crystallization recycling energy saver in acrylonitrile process according to claim 1, it is characterised in that：Thickener
(9) top sets overflow port, overflow port connection mother liquor tank (11), the liquid outlet connection mother liquor tank (11) of centrifuge (10), mother
Flow container (11) connects the bottom of heater (5) by saturated solution feed pump (14).
3. sulphur ammonium crystallization recycling energy saver in acrylonitrile process according to claim 1, it is characterised in that：Crystallizer
(2) middle part sets polymer exit, and polymer exit connects polymer knockout drum (7), polymer point by saturation liquid pump (19)
From tank (7) bottom polymer exit and ammonium sulfate solution is set to export respectively, polymer exit connection polymer buffer tank (8) gathers
It closes object surge tank (8) bottom and waster water incinerator (13), ammonium sulfate solution outlet mother liquor is connected by polymer delivery pump (15)
Surge tank (16), mother liquor surge tank (16) pump the bottom of (17) connection heater (5) by mother liquor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721457284.2U CN207445653U (en) | 2017-11-03 | 2017-11-03 | Sulphur ammonium crystallization recycling energy saver in acrylonitrile process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721457284.2U CN207445653U (en) | 2017-11-03 | 2017-11-03 | Sulphur ammonium crystallization recycling energy saver in acrylonitrile process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207445653U true CN207445653U (en) | 2018-06-05 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107670323A (en) * | 2017-11-03 | 2018-02-09 | 山东齐鲁石化工程有限公司 | Sulphur ammonium crystallization recovery energy saving technique and device in acrylonitrile process |
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2017
- 2017-11-03 CN CN201721457284.2U patent/CN207445653U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107670323A (en) * | 2017-11-03 | 2018-02-09 | 山东齐鲁石化工程有限公司 | Sulphur ammonium crystallization recovery energy saving technique and device in acrylonitrile process |
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