CN2346774Y - Internally circulating carbonators - Google Patents

Internally circulating carbonators Download PDF

Info

Publication number
CN2346774Y
CN2346774Y CN98246741U CN98246741U CN2346774Y CN 2346774 Y CN2346774 Y CN 2346774Y CN 98246741 U CN98246741 U CN 98246741U CN 98246741 U CN98246741 U CN 98246741U CN 2346774 Y CN2346774 Y CN 2346774Y
Authority
CN
China
Prior art keywords
carbonator
tower
utility
model
central
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
CN98246741U
Other languages
Chinese (zh)
Inventor
李武
贺占海
张永胜
吕明远
王文耀
袁玉苹
冯太云
陈靖安
边志富
石光荣
吴永胜
于建平
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.)
Inner Mongolia Yikezhao Chemical Research And Design Institute
Original Assignee
Inner Mongolia Yikezhao Chemical Research And Design Institute
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 Inner Mongolia Yikezhao Chemical Research And Design Institute filed Critical Inner Mongolia Yikezhao Chemical Research And Design Institute
Priority to CN98246741U priority Critical patent/CN2346774Y/en
Application granted granted Critical
Publication of CN2346774Y publication Critical patent/CN2346774Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The utility model relates to an internally circulating carbonator, which belongs to the technical field of chemical equipment. The utility model is characterized in that based on the traditional carbonator, a plurality of sieve plates are arranged at the upper part of the inside of the carbonator; a central circulating cylinder is arranged at the lower part inside the carbonator, and a bacterium cap at the lower part of the carbonator is sheathed in the central circulating cylinder, so the bacterium cap and the carbonator body are partitioned. A CO2 gas inlet pipe is led into the central circulating cylinder, and the carbonator with circulatory flow of external cooling type natural circulation is formed. The utility model mainly for producing sodium bicarbonate has the advantages of stable technological condition, good crystalline grain size, simple operation, long production period and high production capacity.

Description

Internal circulating carbonator
The utility model is a kind of internal circulating carbonator, belongs to the chemical industry equipment field.
The carbonating tower of traditional mode of production sodium bicarbonate generally is that some caps are installed in tower body, at cooling of the bottom of tower body and feeding CO 2Gas.Because this type of tower is at the whole bottom of tower body crystallisation by cooling, thereby its mass-and heat-transfer is poor; Because CO 2Stirring influenced the crystallization of sodium bicarbonate; Also heterodyne of the absorptivity of this tower in addition; This output of column is low in a word.
The purpose of this utility model is to utilize absorptive character, mass-and heat-transfer performance and crystal property, the production cycle of improving carbonating tower to improve the carbonization output of column.
Internal circulating carbonator of the present utility model is at intravital middle part of tower and bottom some caps to be housed; Cooling jacket is equipped with in outer bottom at tower body; Some sieve plates are equipped with on the intravital top of tower; A central circulating barrel is equipped with in the intravital bottom of tower, with the cap of tower body bottom cover therein, separates with tower body; CO 2Gas inlet pipe feeds central circulating barrel; Central authorities' circulation of this internal circulating carbonator is a cylinder type tube.
This internal circulating carbonator is according to crystallization theory and secondary nucleation principle, and the outer cooled carbonating tower with routine is designed to external-cooling type natural circulation carbonating tower, has set up sieve plate in order to strengthen to absorb.This tower utilizes the inside and outside air content difference of central circulating barrel, causes the severe difference as impellent, carries out natural circulation, comes enhancing mass and heat transfer.Simultaneously cooling and absorbing is separated, alleviated cooling section gas violent stirring and destroyed crystalline polamer, the process of cooling degree of supersaturation is even.The stable process conditions of this tower, grain size number is good, simple to operate, the production cycle is long, throughput is big.This tower is mainly used in production sodium bicarbonate.
Figure is the diagrammatic cross-section of the utility model internal circulating carbonator.
Embodiment: (seeing figure)
Internal circulating carbonator of the present utility model is that two-layer sieve plate 2 is equipped with on the top in tower body 1, its middle part and bottom are equipped with 15 caps 3 successively, central authorities' circulating barrel 24 is the cylinder type tube, be contained in the bottom in the tower body 1, and therein with cap 3 cover of tower body 1 bottom, separate with the outer wall of tower body 1, cooling jacket 5, CO are equipped with in the outer bottom of tower body 1 2Gas inlet pipe 6 feeds central circulating barrel 4, and alkali lye import 7, steam outlet 8 and magma outlet 9 are housed respectively in the upper and lower of tower body 1 in addition.During the work of this tower, in cooling jacket 5, feed recirculated cooling water; Alkali lye is sent into CO from tower body 1 top 2Gas is sent into from the bottom, CO 2Gas carries out crystallisation by cooling from central circulating barrel 4 its outer walls of inflow and 1 of tower body after central circulating barrel 4, cap 3 and sieve plate 2 are fully absorbed by alkali lye, magma flows out from the bottom of tower body 1.

Claims (2)

1. the utility model is a kind of internal circulating carbonator, and it is at intravital middle part of tower and bottom some caps to be housed; Cooling jacket is equipped with in outer bottom at tower body; It is characterized in that the intravital top of tower is equipped with some sieve plates; A central circulating barrel is equipped with in the intravital bottom of tower, with the cap of tower body bottom cover therein, separates with tower body; CO 2Gas inlet pipe feeds central circulating barrel.
2. internal circulating carbonator according to claim 1 is characterized in that central authorities' circulation of this internal circulating carbonator is a cylinder type tube.
CN98246741U 1998-11-16 1998-11-16 Internally circulating carbonators Expired - Fee Related CN2346774Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN98246741U CN2346774Y (en) 1998-11-16 1998-11-16 Internally circulating carbonators

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN98246741U CN2346774Y (en) 1998-11-16 1998-11-16 Internally circulating carbonators

Publications (1)

Publication Number Publication Date
CN2346774Y true CN2346774Y (en) 1999-11-03

Family

ID=33992108

Family Applications (1)

Application Number Title Priority Date Filing Date
CN98246741U Expired - Fee Related CN2346774Y (en) 1998-11-16 1998-11-16 Internally circulating carbonators

Country Status (1)

Country Link
CN (1) CN2346774Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110124589A (en) * 2019-05-27 2019-08-16 贵州红星发展股份有限公司 Gas-liquid reaction equipment, its system and the method for preparing barium carbonate using it
CN112266003A (en) * 2020-11-05 2021-01-26 中盐昆山有限公司 Soda ash carbonization tower for combined soda production

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110124589A (en) * 2019-05-27 2019-08-16 贵州红星发展股份有限公司 Gas-liquid reaction equipment, its system and the method for preparing barium carbonate using it
CN112266003A (en) * 2020-11-05 2021-01-26 中盐昆山有限公司 Soda ash carbonization tower for combined soda production
CN112266003B (en) * 2020-11-05 2022-08-05 中盐昆山有限公司 Soda ash carbonization tower for combined soda production

Similar Documents

Publication Publication Date Title
US8287830B2 (en) Devices for preparing ammonium bicarbonate with flue gas and method of using the devices
CN201537456U (en) Flue gas heat exchange type evaporator of flue gas desulfurization side product by ammonia method
CN101135507A (en) Ammonia water absorbing refrigerator
CN100590073C (en) 'Non-combined-soda process' production process for producing soda, ammonium chloride with melamine tail gas
CN2346774Y (en) Internally circulating carbonators
CN102086028A (en) Concentration method for producing highly-concentrated chemical-grade hydrogen peroxide solution
CN207520833U (en) A kind of ammonia-contaminated gas absorption system
CN202237730U (en) Ammonia recycling device for copper washing regenerated gas
CN1333079A (en) Nox containing tail gas processing technology and tower equipment for production of oxalic acid by nitric acid oxidation method
CN209113500U (en) Cold carbonization Tower System outside five one group of tower formulas
CN102659147A (en) Method and device for preparing basic magnesium carbonate from heavy magnesium carbonate water by pyrolysis
CN2868987Y (en) Carbonizing tower for preparing sodium hydrogen carbonate
CN100460051C (en) Double circumfluence composite type reaction device
CN102050447A (en) System for purifying carbon dioxide from combustion tail gas
CN113091338B (en) Reaction heat recycling system in formaldehyde production
CN2915834Y (en) Crystallizer for salt cake separation using freeze method
CN210814844U (en) Stirring and mixing device
CN2620581Y (en) High efficient natural circular external cooling carbonators
CN202415191U (en) Continuous nickel particle dissolving reactor
CN87103005B (en) Carbonization tower cooled externally by natural circulation
CN215832529U (en) Liquid nitrogen gasification cold quantity recovery device for production of four carbon devices
CN220405627U (en) Device for continuously producing dibromoethane
CN214862382U (en) High-efficient refrigerated interior cold type ammonia tower of inhaling
CN220642598U (en) Sulfuric acid process hydrochloric acid analytic system
CN2897991Y (en) System for producing high-concentration carbon-13-carbon dioxide

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee