CN203315766U - Evaporation prilling device for preparing urea - Google Patents

Evaporation prilling device for preparing urea Download PDF

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Publication number
CN203315766U
CN203315766U CN2013204144741U CN201320414474U CN203315766U CN 203315766 U CN203315766 U CN 203315766U CN 2013204144741 U CN2013204144741 U CN 2013204144741U CN 201320414474 U CN201320414474 U CN 201320414474U CN 203315766 U CN203315766 U CN 203315766U
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China
Prior art keywords
evaporation
connects
dual circulation
condenser
prilling device
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.)
Expired - Fee Related
Application number
CN2013204144741U
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Chinese (zh)
Inventor
张书培
冉琳
汪万新
周振洪
郭习文
易志强
刘耀
时兴亚
尹学文
张永旺
陶建彬
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.)
XINJIANG TIANYUN CHEMICAL Co Ltd
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XINJIANG TIANYUN CHEMICAL Co Ltd
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Application filed by XINJIANG TIANYUN CHEMICAL Co Ltd filed Critical XINJIANG TIANYUN CHEMICAL Co Ltd
Priority to CN2013204144741U priority Critical patent/CN203315766U/en
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Publication of CN203315766U publication Critical patent/CN203315766U/en
Anticipated expiration legal-status Critical
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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The utility model relates to the field of chemical engineering, in particular to an evaporation prilling device for preparing urea. The evaporation prilling device for preparing urea comprises an urea tank, wherein the urea tank is connected with an evaporation heater through a pipeline, the evaporation heater is connected with a gas-liquid separator which is provided with a gas pipeline, the gas pipeline is communicated to an evaporative condenser, and a liquid pipeline of the evaporative condenser is connected with the two-stage evaporation heater. Compared with the prior art, the evaporation prilling device with the technical scheme adopted has the advantages of being high in degree of automation, uniform in prilling and high in production speed.

Description

A kind of evaporation prilling device for preparing urea
Technical field
The utility model relates to chemical field, relates in particular to a kind of evaporation prilling device for preparing urea.
Background technology
The urea production automaticity is not high, has affected to a certain extent current industry development.
The utility model content
The purpose of this utility model is to provide the evaporation prilling device for preparing urea that a kind of automaticity is high.
In order to realize above purpose, the utility model adopts following technical scheme: a kind of evaporation prilling device for preparing urea, comprise the urine groove, described urine barrel road connects evaporation heater, described evaporation heater connects gas-liquid separator, gas-liquid separator is provided with gas piping, and described gas piping passes into evaporative condenser, and the liquid line of evaporative condenser connects two-section evaporating heater.
The further technical scheme of the utility model is, described liquid line enters in the tubulation of two-section evaporating heater through U-shaped pipe.
The further technical scheme of the utility model is, after one section evaporation ejector of described evaporative condenser connection, connects final cooler.
The further technical scheme of the utility model is, described two-section evaporating heater connection dual circulation separator.
The further technical scheme of the utility model is, described dual circulation separator connects dual circulation the first condenser, dual circulation the first condenser connects the dual circulation injector, the dual circulation injector connects dual circulation the second condenser, and dual circulation the second condenser connects final cooler by dual circulation the second injector.
The further technical scheme of the utility model is, described dual circulation separator connection granulation tower, and there are scraper and travelling belt in described granulation tower below.
The further technical scheme of the utility model is, also comprises weighing-appliance.
Adopt as above the utility model of technical scheme, with respect to prior art, following beneficial effect is arranged: automaticity is high, granulation is even, and speed of production is fast.
The accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment, wherein: 1 urine groove; 2 evaporation heaters; 3 gas-liquid separators; 4 evaporative condensers; 5 two-section evaporating heaters; 6U type pipe; 7 one sections evaporation ejectors; 8 heat exchange condensers; 9 dual circulation separators; 10 dual circulation the first condensers; 11 dual circulation injectors; 12 dual circulation the second condensers; 13 dual circulation the second injectors; 14 final coolers; 15 Melting pumps; 16 granulation towers; 17 scrapers; 18 weighing-appliances.
The specific embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described, embodiment does not form restriction of the present utility model.
Embodiment
As shown in Figure 1, a kind of evaporation prilling device for preparing urea, comprise urine groove 1, urine groove 1 pipeline connects evaporation heater 2, evaporation heater 2 connects gas-liquid separator 3, gas-liquid separator 3 is provided with gas piping, and gas piping passes into evaporative condenser 4, and the liquid line of evaporative condenser 4 connects two-section evaporating heater 5.The liquid line of evaporative condenser 4 enters in the tubulation of two-section evaporating heater 5 through U-shaped pipe.Evaporative condenser 4 connects one section rear connection final cooler 14 of evaporation ejector 7.Two-section evaporating heater 5 connects dual circulation separator 9.Dual circulation separator 9 connects dual circulation the first condenser 10, dual circulation the first condenser 10 connects dual circulation injector 11, dual circulation injector 11 connects dual circulation the second condenser 12, and dual circulation the second condenser 12 connects final cooler 14 by dual circulation the second injector 13.Dual circulation separator 9 connects granulation tower 16, and there are scraper 17 and travelling belt in granulation tower 16 belows.Also comprise weighing-appliance 18.
The course of work that the present embodiment prepares the evaporation prilling device of urea is:
Be 72% left and right from the urine concentration of urine groove 1, by urine, be pumped into evaporation heater 2 bottoms.
Low-pressure steam makes urine be heated to 130.From evaporation heater 2, gas-liquid mixture out rises to gas-liquid separator 3 and carries out gas-liquid separation, and gas enters in evaporative condenser 4, and liquid is in U-shaped pipe enters the tubulation of two-section evaporating heater 5.Evaporative condenser 4 outlet incoagulable gas are evacuated to final cooler 14 condensations, the vacuum of regulating one section evaporation by one section evaporation ejector 7.
Gas, liquid mixture enter dual circulation separator 9.Gas is delivered in dual circulation the first condenser 10 through stepup transformer, uncooled gas is evacuated in dual circulation the second condenser 12 by dual circulation injector 11, wherein uncondensed gas is evacuated to condensation in final cooler 14 by dual circulation the second injector 13 again, after drain into chimney.Enter system by regulating a certain amount of air, can regulate the vacuum of dual circulation.
Evaporative condenser 4 is by the recirculated water heat exchange, and the ammoniacal liquor of condensation enters in each different cell of ammonia vessel.
From the dual circulation separator, concentration out is 99.7% fusing urea, is delivered to the prilling spry at granulation tower 16 tops by Melting pump 15.While stopping granulation, during urine is returned via triple valve; Start can pass into steam condensate clean cycle pipeline after granulation.After the urine ejection entered, the air entered at the bottom of tower is cooling.Fall the urea granules that column bottom temperature is about 70, scraped into blanking groove by scraper 17, after the granulation tower belt is sent into equipment 18 and is weighed directly to the finished product packing building.

Claims (7)

1. an evaporation prilling device for preparing urea, it is characterized in that, comprise urine groove (1), described urine groove (1) pipeline connects evaporation heater (2), described evaporation heater (2) connects gas-liquid separator (3), gas-liquid separator (3) is provided with gas piping, and described gas piping passes into evaporative condenser (4), and the liquid line of evaporative condenser (4) connects two-section evaporating heater (5).
2. a kind of evaporation prilling device for preparing urea according to claim 1, is characterized in that, described liquid line enters in the tubulation of two-section evaporating heater (5) through U-shaped pipe.
3. a kind of evaporation prilling device for preparing urea according to claim 1, is characterized in that, described evaporative condenser (4) connects final cooler (14) after connecting one section evaporation ejector (7).
4. a kind of evaporation prilling device for preparing urea according to claim 1, is characterized in that, described two-section evaporating heater (5) connects dual circulation separator (9).
5. a kind of evaporation prilling device for preparing urea according to claim 4, it is characterized in that, described dual circulation separator (9) connects dual circulation the first condenser (10), dual circulation the first condenser (10) connects dual circulation injector (11), dual circulation injector (11) connects dual circulation the second condenser (12), and dual circulation the second condenser (12) connects final cooler (14) by dual circulation the second injector (13).
6. a kind of evaporation prilling device for preparing urea according to claim 4, is characterized in that, described dual circulation separator (9) connects granulation tower (16), and there are scraper (17) and travelling belt in described granulation tower (16) below.
7. a kind of evaporation prilling device for preparing urea according to claim 6, is characterized in that, also comprises weighing-appliance.
CN2013204144741U 2013-07-11 2013-07-11 Evaporation prilling device for preparing urea Expired - Fee Related CN203315766U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2013204144741U CN203315766U (en) 2013-07-11 2013-07-11 Evaporation prilling device for preparing urea

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2013204144741U CN203315766U (en) 2013-07-11 2013-07-11 Evaporation prilling device for preparing urea

Publications (1)

Publication Number Publication Date
CN203315766U true CN203315766U (en) 2013-12-04

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2013204144741U Expired - Fee Related CN203315766U (en) 2013-07-11 2013-07-11 Evaporation prilling device for preparing urea

Country Status (1)

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CN (1) CN203315766U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105417602A (en) * 2015-11-23 2016-03-23 河南心连心化肥有限公司 Large granulated urea device liquid waste treatment device and treatment method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105417602A (en) * 2015-11-23 2016-03-23 河南心连心化肥有限公司 Large granulated urea device liquid waste treatment device and treatment method
CN105417602B (en) * 2015-11-23 2018-02-13 河南心连心化肥有限公司 Large granule urea plant liquid waste treating apparatus and processing method

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20131204

Termination date: 20170711

CF01 Termination of patent right due to non-payment of annual fee