CN203315975U - Improved large-size internal-cooling ammonia absorption tower - Google Patents

Improved large-size internal-cooling ammonia absorption tower Download PDF

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Publication number
CN203315975U
CN203315975U CN2013203480590U CN201320348059U CN203315975U CN 203315975 U CN203315975 U CN 203315975U CN 2013203480590 U CN2013203480590 U CN 2013203480590U CN 201320348059 U CN201320348059 U CN 201320348059U CN 203315975 U CN203315975 U CN 203315975U
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CN
China
Prior art keywords
tower
liquid
water tank
ammonia
distributor
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 - Lifetime
Application number
CN2013203480590U
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Chinese (zh)
Inventor
鲁泳
常红林
刘钊飞
张忠杰
王春凡
李树旺
康林勇
李宝新
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.)
Tianjin Bohua Yongli Chemical Industry Co ltd
Original Assignee
TIANJIN ALKALI PLANT BOHAI CHEMICAL CO Ltd TIANJIN
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 TIANJIN ALKALI PLANT BOHAI CHEMICAL CO Ltd TIANJIN filed Critical TIANJIN ALKALI PLANT BOHAI CHEMICAL CO Ltd TIANJIN
Priority to CN2013203480590U priority Critical patent/CN203315975U/en
Application granted granted Critical
Publication of CN203315975U publication Critical patent/CN203315975U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model discloses an improved large-size internal-cooling ammonia absorption tower which comprises a tower ring, a bubble-cap plate, a cooling water tank, a liquid distributor and a liquid redistributor, wherein the liquid distributor is provided with a gas lift pipe and a downcomer; the tower ring positioned under the cooling water tank is provided with a gas inlet and a liquid outlet; a gasket is arranged between the liquid distributor and the tower ring; and the gas inlet extends towards the inside of the tower to the middle part of the tower, and is arranged downwards to form an ammonia gas distributor. In the utility model, the gasket is added to the bottom of the liquid distributor solves the problem of liquid leakage in the liquid distributor, and enhances the ammonia absorption effect of the dilute ammoniacal brine. The gas inlet extends towards the inside of the tower to the middle part of the tower, and is arranged downwards to form the ammonia gas distributor, thereby solving the problem of liquid leakage since the ammonia gas directly erodes the connecting pipe of the water tank, and uniformly cooling the ammonia gas in the tower through the water tank.

Description

A kind of improved large-scale internal cooling type ammonia adsoption tower
Technical field
The utility model relates to a kind of efficient absorption equipment in the soda ash production process, and the utility model relates in particular to ammonia absorption tower.
Background technology
Ammonia absorption tower is that the refined brine that a kind of use is removed calcium, magnesium and salt slurry absorbs the NH distill from the alkaline filtrated stock 3And CO 2Gas, thereby make intermediate products---the equipment of-ammonial brine, in denomination of invention, be " a kind of large-scale internal cooling type ammonia adsoption tower ", the patent No. is CN03258432.6, the Chinese patent that the applying date is on September 12nd, 2003 discloses a kind of internal cooling type ammonia adsoption tower, this equipment has improved single tower production capacity, with the outer cooling tower simplified in comparison cooling process, improved production efficiency.But occurred that in continuous flow procedure liquid distribution trough leakage, the air inlet of ammonia air inlet cause the problems such as water tank leakage.
Summary of the invention
The purpose of this utility model is to overcome the deficiency of prior art, and a kind of solution leakage problem is provided, and guarantees stable and successional a kind of improved large-scale internal cooling type ammonia adsoption tower of producing.
A kind of improved large-scale internal cooling type ammonia adsoption tower of the present utility model, it comprises tower circle, bubble cap plate, cooling water tank, liquid distribution trough, liquid re-distributor, be provided with air-lift tube and downspout on described liquid distribution trough, have air inlet and liquid outlet on tower circle below being positioned at described cooling water tank, be provided with packing ring between described liquid distribution trough and tower circle, described air inlet extends to the tower middle part and formation ammonia distributor is set downwards in tower.
Increase packing ring in the liquid distribution trough bottom in the utility model and solve liquid distribution trough leakage problem, strengthen light ammonial brine and inhale the ammonia effect.In the utility model device, air inlet is extended to the tower middle part in tower, and form the ammonia distributor downwards, solve because adapter place of the direct erosion water tank of ammonia causes the leakage problem, and make the interior ammonia of tower evenly cooling by water tank.
The accompanying drawing explanation
Accompanying drawing is the structural representation of a kind of improved large-scale internal cooling type ammonia adsoption tower of the present utility model.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in detail.
A kind of improved large-scale internal cooling type ammonia adsoption tower of the present utility model as shown in drawings, it comprises tower circle 1, bubble cap plate 2, cooling water tank 3, liquid distribution trough 6, liquid re-distributor 7, be provided with air-lift tube 8 and downspout 9 on described liquid distribution trough, have air inlet 4 and liquid outlet 5 on tower circle below being positioned at described cooling water tank, be provided with packing ring 11 between described liquid distribution trough and tower circle, described air inlet extends to the tower middle part and formation ammonia distributor 12 is set downwards in tower.
Internal cooling type ammonia adsoption tower is comprised of a plurality of tower circles 1, and top is washing section; Middle part, for absorption, cooling section, is provided with cooling water tank 3, and has air inlet 4 and liquid outlet 5 on the foundation ring below cooling water tank 3 on its tower body, ammonial brine storage tank 10 can be accepted in the tower bottom.
Refined brine is entered through bubble cap plate by the washing section on top, the NH in washing, absorption tail gas 3And CO 2, then by brine distribution device and salt solution redistributor evenly the salt solution sprinkle is absorbed in middle part, cooling section is arranged in the middle of cooling water tank, gas and liquid drive in the wrong direction, the outside wall surface of cooling water tank, heat transfer and mass transfer carry out simultaneously.
The easy leakage of the liquid distribution trough of original equipment and the edge of equipment connection, light ammonial brine is not had all by the downspout of distributor, make light ammonial brine skewness, the ammonia effect is inhaled in impact, by optimizing distributor designs, increase packing ring in the liquid distribution trough bottom and solve liquid distribution trough leakage problem, strengthen light ammonial brine and inhale the ammonia effect.
After the ammonia of original equipment enters ammonia absorption tower by air inlet 4, because flow velocity is larger, easily erosion water tank adapter place and cause leakage, in the utility model device, air inlet 4 is extended to the tower middle part in tower, and form the ammonia distributor downwards, solution causes the leakage problem because of adapter place of the direct erosion water tank of ammonia, and makes the interior ammonia of tower evenly cooling by water tank.

Claims (1)

1. an improved large-scale internal cooling type ammonia adsoption tower, it comprises tower circle, bubble cap plate, cooling water tank, liquid distribution trough, liquid re-distributor, be provided with air-lift tube and downspout on described liquid distribution trough, have air inlet and liquid outlet on tower circle below being positioned at described cooling water tank, it is characterized in that: be provided with packing ring between described liquid distribution trough and tower circle, described air inlet extends to the tower middle part and formation ammonia distributor is set downwards in tower.
CN2013203480590U 2013-06-17 2013-06-17 Improved large-size internal-cooling ammonia absorption tower Expired - Lifetime CN203315975U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2013203480590U CN203315975U (en) 2013-06-17 2013-06-17 Improved large-size internal-cooling ammonia absorption tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2013203480590U CN203315975U (en) 2013-06-17 2013-06-17 Improved large-size internal-cooling ammonia absorption tower

Publications (1)

Publication Number Publication Date
CN203315975U true CN203315975U (en) 2013-12-04

Family

ID=49655377

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2013203480590U Expired - Lifetime CN203315975U (en) 2013-06-17 2013-06-17 Improved large-size internal-cooling ammonia absorption tower

Country Status (1)

Country Link
CN (1) CN203315975U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110745846A (en) * 2019-11-11 2020-02-04 衡阳凯美科化工有限公司 Ammonia absorption ejector for soda production

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110745846A (en) * 2019-11-11 2020-02-04 衡阳凯美科化工有限公司 Ammonia absorption ejector for soda production

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee
CP03 Change of name, title or address

Address after: 300450 No. ten, No. 3369, Tanggu Lingang Industrial Zone, Tanggu District, Tianjin, Bohai

Patentee after: TIANJIN BOHUA YONGLI CHEMICAL INDUSTRY Co.,Ltd.

Address before: 300450, No. ten, No. 3369, Bohai Lingang Industrial Zone, Tanggu District, Tianjin, Tianjin, Tanggu

Patentee before: Tianjin Soda Plant, Tianjin Bohai Chemical Industry Co.,Ltd.

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20131204