CN204509190U - Equipment derived by a kind of new Type Coke Oven raw gas - Google Patents

Equipment derived by a kind of new Type Coke Oven raw gas Download PDF

Info

Publication number
CN204509190U
CN204509190U CN201520049866.1U CN201520049866U CN204509190U CN 204509190 U CN204509190 U CN 204509190U CN 201520049866 U CN201520049866 U CN 201520049866U CN 204509190 U CN204509190 U CN 204509190U
Authority
CN
China
Prior art keywords
upcast
effuser
bridge tube
raw gas
brick
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
CN201520049866.1U
Other languages
Chinese (zh)
Inventor
邢同春
邢斌
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201520049866.1U priority Critical patent/CN204509190U/en
Application granted granted Critical
Publication of CN204509190U publication Critical patent/CN204509190U/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

  • Industrial Gases (AREA)

Abstract

The utility model relates to coal oven dithio-gas and utilizes field, and equipment derived by especially a kind of new Type Coke Oven raw gas.It comprises: steel frame, upcast, upcast bridge tube, the brick gas passage surrounded by fireclay brick, effuser bridge tube and effuser, described brick gas passage and effuser are all installed on steel frame, described brick gas passage is connected with upcast by upcast bridge tube, described effuser is connected with upcast by effuser bridge tube, be provided with upcast bridge tube flap valve in described upcast bridge tube, in described effuser bridge tube, be provided with effuser bridge tube water seal flap valve.It can intercept raw gas high temperature sensible heat, and the superheated vapour of production high-quality generates electricity, and reclaims raw gas reaches synergy consumption reduction object to UTILIZATION OF VESIDUAL HEAT IN; There is the function that raw gas is derived; Brick gas line has adiabatic heat-insulation function; Effuser has washing heat exchange to raw gas, removes the function of the coal-tar middle oil and impurity of raw gas.

Description

Equipment derived by a kind of new Type Coke Oven raw gas
Technical field
The utility model relates to coal oven dithio-gas and utilizes field, and equipment derived by especially a kind of new Type Coke Oven raw gas.
Background technology
It is derived by the upcast on coke furnace carbonization chamber top that domestic and foreign current coal oven dithio-gas derives equipment, enters effuser, complete and ammonia scrubbing heat transfer process in effuser by bridge tube raw gas.About 85-89 DEG C is cooled to by the raw gas temperatures of about 650 DEG C.Cooled raw gas flows to gas-liquid separator along raw coke oven gas pipeline together with ammoniacal liquor and coal tar, and coal gas enters purification section from gas-liquid separator upper pipe, and coal tar ammoniacal liquor carries out ammoniacal liquor separation along lower pipeline after flowing into mechanical settling tank.
Although people have carried out many discussions to the sensible heat utilization of raw gas for many years, adopt the upcast of traditional structure derivation mode to reclaim crude-gas sensible heat and be difficult to realize.
Utility model content
The utility model is intended to solve the problem, and provide a kind of new Type Coke Oven raw gas and derive equipment, it can intercept raw gas high temperature sensible heat, and the superheated vapour of production high-quality generates electricity, and reclaims raw gas reaches synergy consumption reduction object to UTILIZATION OF VESIDUAL HEAT IN; There is the function that raw gas is derived; Brick gas line has adiabatic heat-insulation function; Effuser has washing heat exchange to raw gas, removes the function of the coal-tar middle oil and impurity of raw gas, and its technical scheme adopted is as follows:
Equipment derived by a kind of new Type Coke Oven raw gas, it is characterized in that, comprise: steel frame, upcast, upcast bridge tube, the brick gas passage surrounded by fireclay brick, effuser bridge tube and effuser, described brick gas passage and effuser are all installed on steel frame, described brick gas passage is connected with upcast by upcast bridge tube, described effuser is connected with upcast by effuser bridge tube, upcast bridge tube flap valve is provided with in described upcast bridge tube, effuser bridge tube water seal flap valve is provided with in described effuser bridge tube, described effuser top is provided with can to the ammoniacal liquor shower nozzle of the inner sprinkle ammoniacal liquor of effuser.
On technique scheme basis, described brick gas passage periphery is provided with insulation thermal insulation layer.
On technique scheme basis, described upcast top has the upcast clean-out opening for cleaning upcast inner chamber, described upcast bridge tube having the bridge tube clean-out opening for cleaning upcast bridge tube inner chamber, described brick gas passage having the brick gas passage clean-out opening for cleaning brick gas passage inner chamber.
On technique scheme basis, described effuser bridge tube is provided with aerobic water shower nozzle, described aerobic water shower nozzle is positioned at the top of effuser bridge tube water seal flap valve.
The utility model tool has the following advantages: can intercept raw gas high temperature sensible heat, the superheated vapour of production high-quality generates electricity, and reclaims raw gas reaches synergy consumption reduction object to UTILIZATION OF VESIDUAL HEAT IN; There is the function that raw gas is derived; Brick gas line has adiabatic heat-insulation function; Effuser has washing heat exchange to raw gas, removes the function of the coal-tar middle oil and impurity of raw gas.
Accompanying drawing explanation
Fig. 1: cross-sectional view of the present utility model;
Embodiment
Below in conjunction with accompanying drawing and example, the utility model is described in further detail:
As shown in Figure 1, equipment derived by a kind of new Type Coke Oven raw gas of the present embodiment, it is characterized in that, comprise: steel frame 5, upcast 2, upcast bridge tube 9, the brick gas passage 3 surrounded by fireclay brick 13, effuser bridge tube 15 and effuser 4, upcast 2 is cylinder, for heat resisting brick builds lining by laying bricks or stones in cylindrical shell, outside cylindrical shell is that cast steel or cast iron quality are formed, its root 7 is installed on oven top of coke oven 1, described brick gas passage 3 and effuser 4 are all installed on steel frame 5, described brick gas passage 3 is connected with upcast 2 by upcast bridge tube 9, described effuser 4 is connected with upcast 2 by effuser bridge tube 15, upcast bridge tube flap valve 10 is provided with in described upcast bridge tube 9, upcast bridge tube flap valve 10 material can be cast iron, be provided with effuser bridge tube water seal flap valve 17 in described effuser bridge tube 15, the keying of effuser bridge tube water seal flap valve 17 is controlled by water seal flap valve handle 18, and described effuser 4 top is provided with can to the ammoniacal liquor shower nozzle 19 of the inner sprinkle ammoniacal liquor of effuser 4.
Preferably, described brick gas passage 3 periphery is provided with insulation thermal insulation layer 14, its objective is and prevents raw gas excessive drop temperature in brick gas passage 3.
Preferably, described upcast 2 top has the upcast clean-out opening 8 for cleaning upcast 2 inner chamber, described upcast bridge tube 9 having the bridge tube clean-out opening 11 for cleaning upcast bridge tube 9 inner chamber, described brick gas passage 3 having the brick gas passage clean-out opening 12 for cleaning brick gas passage 3 inner chamber.
Further, described effuser bridge tube 15 is provided with aerobic water shower nozzle 16, described aerobic water shower nozzle 16 is positioned at the top of effuser bridge tube water seal flap valve 17.
When intercepting crude-gas sensible heat and producing superheated vapour, open the upcast bridge tube flap valve 10 closure set tracheae bridge tube water seal flap valve 17 in upcast bridge tube 9, now raw gas enters brick gas passage through upcast, upcast bridge tube 9, enters residual heat boiler for exchanging heat along brick gas passage.Brick gas passage guarantees that raw gas temperature reduces cooling before entering waste heat boiler, makes it keep higher temperature (to be not less than 650 ° c), in order that the superheated vapour of production higher quality.
When waste heat boiler need stop production to overhaul or break down need stop production time, effuser bridge tube water seal flap valve 17 can be opened, close upcast bridge tube flap valve 10, after now raw gas enters lower the temperature with ammoniacal liquor heat exchange in effuser 4 along effuser bridge tube 15, raw gas enters cleaning shop through air water separator.
The new Type Coke Oven raw gas derivation equipment of the application both can reclaim crude-gas sensible heat production superheated vapour and go generating, did not affect again the normal production operation of coke oven, had reclaimed crude-gas sensible heat, reduced gas consumption.
Be illustrated the utility model by way of example above, but the utility model is not limited to above-mentioned specific embodiment, all any changes of doing based on the utility model or modification all belong to the claimed scope of the utility model.

Claims (4)

1. equipment derived by a new Type Coke Oven raw gas, it is characterized in that, comprise: steel frame (5), upcast (2), upcast bridge tube (9), the brick gas passage (3) surrounded by fireclay brick (13), effuser bridge tube (15) and effuser (4), described brick gas passage (3) and effuser (4) are all installed on steel frame (5), described brick gas passage (3) is connected with upcast (2) by upcast bridge tube (9), described effuser (4) is connected with upcast (2) by effuser bridge tube (15), upcast bridge tube flap valve (10) is provided with in described upcast bridge tube (9), effuser bridge tube water seal flap valve (17) is provided with in described effuser bridge tube (15), described effuser (4) top is provided with can to the ammoniacal liquor shower nozzle (19) of the inner sprinkle ammoniacal liquor of effuser (4).
2. equipment derived by a kind of new Type Coke Oven raw gas according to claim 1, it is characterized in that: described brick gas passage (3) periphery is provided with insulation thermal insulation layer (14).
3. equipment derived by a kind of new Type Coke Oven raw gas according to claim 1 and 2, it is characterized in that: described upcast (2) top has the upcast clean-out opening (8) for cleaning upcast (2) inner chamber, described upcast bridge tube (9) having the bridge tube clean-out opening (11) for cleaning upcast bridge tube (9) inner chamber, described brick gas passage (3) having the brick gas passage clean-out opening (12) for cleaning brick gas passage (3) inner chamber.
4. equipment derived by a kind of new Type Coke Oven raw gas according to claim 3, it is characterized in that: described effuser bridge tube (15) is provided with aerobic water shower nozzle (16), and described aerobic water shower nozzle (16) is positioned at the top of effuser bridge tube water seal flap valve (17).
CN201520049866.1U 2015-01-20 2015-01-20 Equipment derived by a kind of new Type Coke Oven raw gas Expired - Fee Related CN204509190U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520049866.1U CN204509190U (en) 2015-01-20 2015-01-20 Equipment derived by a kind of new Type Coke Oven raw gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520049866.1U CN204509190U (en) 2015-01-20 2015-01-20 Equipment derived by a kind of new Type Coke Oven raw gas

Publications (1)

Publication Number Publication Date
CN204509190U true CN204509190U (en) 2015-07-29

Family

ID=53707184

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520049866.1U Expired - Fee Related CN204509190U (en) 2015-01-20 2015-01-20 Equipment derived by a kind of new Type Coke Oven raw gas

Country Status (1)

Country Link
CN (1) CN204509190U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110452714A (en) * 2019-08-17 2019-11-15 河北科技大学 A kind of coal oven dithio-gas high temperature withdrawing device and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110452714A (en) * 2019-08-17 2019-11-15 河北科技大学 A kind of coal oven dithio-gas high temperature withdrawing device and method

Similar Documents

Publication Publication Date Title
CN103436272B (en) Ascending pipe heat exchange device for raw gas of coke oven
CN102559289B (en) Biomass synthesis gas cooling and washing process and system
CN101701703B (en) Residual heat utilizing technology of coke oven crude gas
CN103666583A (en) Waste heat boiler device of entrained bed gasifier
CN203797614U (en) Heat recovery boiler for cooling biomass synthesis gas to generate electricity
CN204509192U (en) A kind of coke oven coke oven uprising tube heat exchange heat-energy recovering apparatus
CN203530218U (en) Heat transfer device of raw coke oven gas ascension pipe of coke oven
CN109022789B (en) Titanium sponge reduction distillation system with straight passageway
CN204079874U (en) Riser waste heat recovery device for coke oven
CN203668308U (en) Unit type coke oven ascending pipe waste heat recovery device
CN102899057A (en) Heat exchanger for recovering waste heat of raw gas of ascension pipe of coke oven
CN204509190U (en) Equipment derived by a kind of new Type Coke Oven raw gas
CN203559031U (en) Waste pot device of entrained-flow bed gasification furnace
CN204824714U (en) Coke oven crude gas waste heat recovery heat transfer device
CN105779672B (en) It is a kind of for controlling the stopper of molten slag flow
CN204174178U (en) Multi-nozzle coal slurry gasifier
CN206607195U (en) Raw coke oven gas tedge heat sink
CN202643628U (en) Heat exchange-type ascending tube and coke oven
CN102786953B (en) Coke oven grouped novel bridge pipe crude gas waste heat recovery device
CN104728821A (en) Ascending pipe raw gas waste heat utilizing boiler system
CN104694139A (en) Coke oven raw gas heat exchanger with flow guide device
CN204786295U (en) Tedge raw coke oven gas waste heat utilization boiler system
CN204079873U (en) Upcast heat-exchanger rig
CN204923970U (en) Long service life's coke oven crude gas waste heat recovery heat transfer device
CN202881180U (en) Heat exchanger of crude gas waste heat recovery used for coke oven ascension pipe

Legal Events

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

Granted publication date: 20150729