CN204806353U - Retrieve equipment of tedge waste heat - Google Patents

Retrieve equipment of tedge waste heat Download PDF

Info

Publication number
CN204806353U
CN204806353U CN201520292783.5U CN201520292783U CN204806353U CN 204806353 U CN204806353 U CN 204806353U CN 201520292783 U CN201520292783 U CN 201520292783U CN 204806353 U CN204806353 U CN 204806353U
Authority
CN
China
Prior art keywords
tedge
annular
bridge tube
tubulation
toroidal shell
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
CN201520292783.5U
Other languages
Chinese (zh)
Inventor
王平山
文海波
姜龙龙
刘小源
朱友光
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.)
XUZHOU TENGDA COKING CO., LTD.
Original Assignee
XUZHOU WEITIAN CHEMCIAL CO 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 XUZHOU WEITIAN CHEMCIAL CO Ltd filed Critical XUZHOU WEITIAN CHEMCIAL CO Ltd
Priority to CN201520292783.5U priority Critical patent/CN204806353U/en
Application granted granted Critical
Publication of CN204806353U publication Critical patent/CN204806353U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Coke Industry (AREA)

Abstract

The utility model discloses a retrieve equipment of tedge waste heat, including upper portion tedge, tedge tube cap, bridge tube and discharge, bridge tube one end and bridge tube flange joint, the other end is connected with the discharge, still includes annular casing, and annular casing setting is between upper portion tedge and tedge tube cap, and annular casing passes through the bridge tube flange to be connected with the bridge tube, the annular housing face annular tubulation that distributes, and annular tubulation is connected with the steam pocket, and annular casing is " eight " font and describes. The high temperature raw coke oven gas gets into the internal portion of circular casing by the upper portion tedge, upwards flow to top back -porch annular shells inner wall downwards to bridge tube department because the effect of aqueous ammonia spray line, the negative pressure sucks in the discharge, flow the in -process raw coke oven gas through annular casing and annular tubulation heat transfer, annular tubulation is heat transfer to steam pocket, byproduct steam or hot water, make full use of the high temperature raw coke oven gas, the while has still avoided appearing heat pipe booster, the overheated coking scheduling problem of conduction oil.

Description

Reclaim the equipment of tedge waste heat
Technical field
The utility model relates to a kind of waste heat recovery apparatus, is specifically related to a kind of equipment reclaiming tedge waste heat.
Background technology
In recent years along with the lasting propelling to the work of coking industry energy-saving consumption reduction, the energy waste how solved in production process also more and more obtains the attention of people.Coke enterprise is since use carbonizing chamber method fires coke, and in tedge, the waste heat of high temperature coke oven raw coke oven gas just fails effectively to utilize always, with cyclic ammonia water cooling, heat can only be wasted.Someone is by the processing medium water heat exchange in raw coke oven gas and chuck, but occurs heat-transfer surface bonding tar, floccule blockage problem, and after heat-transfer surface damages, in chuck, processing medium water leaks and affects coke production into carbonizing chamber.In recent years, hot pipe technique and conduction oil technology is adopted to carry out waste heat of coke oven crude gas utilization, all can not long-period stable operation, main cause is: these technology all do not overcome the difficulty of coke-stove gas heat exchange, when heat-exchange system other parts fault quits work, carbonizing chamber method, an oven coke has not been produced, can not blowing out within the short time of midway, so there is the problem such as heat pipe booster, the overheated coking of conduction oil.
Summary of the invention
For above-mentioned prior art Problems existing, the utility model provides a kind of equipment reclaiming tedge waste heat, takes full advantage of high temperature raw coke oven gas, also avoid simultaneously and occurs the problem such as heat pipe booster, the overheated coking of conduction oil.
To achieve these goals, the technical solution adopted in the utility model is: a kind of equipment reclaiming tedge waste heat, comprise top tedge, tedge pipe lid, bridge tube and discharge, bridge tube one end and bridge tube Flange joint, the other end is connected with discharge, also comprise toroidal shell, toroidal shell is arranged between top tedge and tedge pipe lid, toroidal shell is connected with bridge tube by bridge tube flange, toroidal shell surface distributed annular tubulation, annular tubulation is connected with drum, and toroidal shell is "eight" shape shape.
Further, toroidal shell is constantly expanded by top-to-bottom caliber, and bottom tilts to bridge tube closure.
Further, annular tubulation adopts built-up welding mode to be connected with toroidal shell.
The beneficial effects of the utility model are: high temperature raw coke oven gas enters toroidal shell inside by top tedge, travel up to behind top that annularly inner walls is down to bridge tube place, and due to the effect of ammoniacal liquor spray line, negative pressure sucks in discharge; In flow process, raw coke oven gas is by toroidal shell and annular tubulation heat exchange, and heat is passed to drum by annular tubulation, byproduct steam or hot water, takes full advantage of high temperature raw coke oven gas, also avoid simultaneously and occurs the problem such as heat pipe booster, the overheated coking of conduction oil.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
In figure: 1, drum, 2, tedge pipe lid, 3, toroidal shell, 4, annular tubulation, 5, bridge tube flange, 6, bridge tube, 7, top tedge, 8, discharge, 9, ammoniacal liquor spray line.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1, the equipment of this recovery tedge waste heat, comprise top tedge 7, tedge pipe lid 2, bridge tube 6 and discharge 8, bridge tube 6 one end is connected with bridge tube flange 5, the other end is connected with discharge 8, also comprise toroidal shell 3, toroidal shell 3 is arranged between top tedge 7 and tedge pipe lid 2, toroidal shell 3 is connected with bridge tube 6 by bridge tube flange 5, toroidal shell 3 surface distributed annular tubulation 4, annular tubulation 4 is connected with drum 1, toroidal shell 3 is "eight" shape shape, heat exchange area in toroidal shell 3 can be increased, toroidal shell 3 is constantly expanded by top-to-bottom caliber, bottom tilts to bridge tube 6 closure, attachment tar graphite is trickled along inwall.In order to improve the utility model performance, annular tubulation 4 adopts built-up welding mode to be connected with toroidal shell 3.
During work, it is inner that high temperature raw coke oven gas enters toroidal shell 3 by top tedge 7, travels up to behind top that annularly housing 3 inwall is down to bridge tube 6 place, and because ammoniacal liquor spray line 9 acts on, negative pressure sucks in discharge 8.In flow process, raw coke oven gas is by toroidal shell 3 and the heat exchange of annular tubulation 4, and heat is passed to drum 1 by annular tubulation 4, byproduct steam or hot water.

Claims (3)

1. one kind is reclaimed the equipment of tedge waste heat, comprise top tedge (7), tedge pipe lid (2), bridge tube (6) and discharge (8), bridge tube (6) one end is connected with bridge tube flange (5), the other end is connected with discharge (8), it is characterized in that, also comprise toroidal shell (3), toroidal shell (3) is arranged between top tedge (7) and tedge pipe lid (2), toroidal shell (3) is connected with bridge tube (6) by bridge tube flange (5), toroidal shell (3) surface distributed annular tubulation (4), annular tubulation (4) is connected with drum (1), toroidal shell (3) is "eight" shape shape.
2. a kind of equipment reclaiming tedge waste heat according to claim 1, is characterized in that, described toroidal shell (3) is constantly expanded by top-to-bottom caliber, and bottom tilts to bridge tube (6) closure.
3. a kind of equipment reclaiming tedge waste heat according to claim 1, is characterized in that, described annular tubulation (4) adopts built-up welding mode to be connected with toroidal shell (3).
CN201520292783.5U 2015-05-08 2015-05-08 Retrieve equipment of tedge waste heat Expired - Fee Related CN204806353U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520292783.5U CN204806353U (en) 2015-05-08 2015-05-08 Retrieve equipment of tedge waste heat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520292783.5U CN204806353U (en) 2015-05-08 2015-05-08 Retrieve equipment of tedge waste heat

Publications (1)

Publication Number Publication Date
CN204806353U true CN204806353U (en) 2015-11-25

Family

ID=54591171

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520292783.5U Expired - Fee Related CN204806353U (en) 2015-05-08 2015-05-08 Retrieve equipment of tedge waste heat

Country Status (1)

Country Link
CN (1) CN204806353U (en)

Similar Documents

Publication Publication Date Title
CN103131432B (en) Method for recovering waste heat from coke oven raw gas
CN204779463U (en) Coke oven tedge waste heat recovery apparatus
CN104214990B (en) A kind of coal oven dithio-gas sensible heat reclaims water refrigeration system and method
CN204824714U (en) Coke oven crude gas waste heat recovery heat transfer device
CN204806353U (en) Retrieve equipment of tedge waste heat
CN204874564U (en) Blast furnace slag water waste heat recovery device
CN204079875U (en) A kind of new Type Coke Oven raw gas waste-heat recovery device
CN203928768U (en) A kind of slag cooler that adopts water pipe
CN112503975A (en) Shell and tube type three-phase heat exchanger
CN207645815U (en) A kind of Slapple activating furnace energy conserving system
CN203053260U (en) Gas and water mixer
CN211522135U (en) Device for heating rich oil and removing benzene by using waste heat of coke oven ascending pipe
CN207811662U (en) A kind of waste heat of coke oven crude gas recovery system based on power-saving technology
CN204058006U (en) A kind of device of coal gas waste heat recovery
CN207091373U (en) A kind of multistage hold over system
CN106016817A (en) Carbon dioxide recovery device based on open type absorption refrigeration cycle
CN104832909A (en) Heat recovery device for removing dust coke powder through coke dry quenching and heat recovery process thereof
CN205299577U (en) Remove dioxin device
CN104477955A (en) Novel vapor condensate water temperature reduction and heat reclaim method in aluminum oxide production
CN202993929U (en) Heat exchanger of ascension pipe of coke oven
CN208200831U (en) A kind of coke oven coke oven uprising tube raw coke oven gas residual heat using device
CN203319940U (en) Novel energy-saving process device for producing chemical feed gas
CN203413988U (en) 180-degree shell-tube type heat exchanging unit and 180-degree shell-tube type heat exchanging device for gathering, transportation and heat tracing of oil field
CN211476803U (en) Shell and tube type three-phase heat exchanger
CN220951640U (en) Coke oven gas collecting tube waste heat utilization device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20160620

Address after: 221000 metallurgical industry agglomeration area, Qingshan Town, Jiawang District, Xuzhou, Jiangsu

Patentee after: XUZHOU TENGDA COKING CO., LTD.

Address before: Copper Mt. District 221000 of Jiangsu city of Xuzhou Province Li Guo Zhen Ma Yuan Cun

Patentee before: Xuzhou Weitian Chemcial Co., Ltd.

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

Granted publication date: 20151125

Termination date: 20200508

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