CN202558653U - Slag discharging device of ammonia still - Google Patents
Slag discharging device of ammonia still Download PDFInfo
- Publication number
- CN202558653U CN202558653U CN2011203920322U CN201120392032U CN202558653U CN 202558653 U CN202558653 U CN 202558653U CN 2011203920322 U CN2011203920322 U CN 2011203920322U CN 201120392032 U CN201120392032 U CN 201120392032U CN 202558653 U CN202558653 U CN 202558653U
- Authority
- CN
- China
- Prior art keywords
- pipe
- valve
- steam
- slag discharging
- communicated
- 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
Links
Images
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
Landscapes
- Beans For Foods Or Fodder (AREA)
Abstract
The utility model discloses a slag discharging device of an ammonia still. The slag discharging device comprises an ammonia still body, a slag discharging pipe, a steam pipe, a steam jacket pipe, a condensate water recycling pipe, a slag discharging valve, a steam blowing valve, a jacket heating valve, a heat insulation plug valve and a drain valve. The slag discharging pipe is communicated with the bottom of the ammonia still body, the slag discharging valve is arranged on the slag discharging pipe, the steam blowing valve is communicated onto the slag discharging pipe on the lower portion of the slag discharging valve, one end of the steam blowing valve is communicated with the steam pipe, the tail end of the slag discharging pipe is connected with a slag tank, the steam jacket pipe is arranged on the outer layer of the slag discharging pipe, the heat insulation plug valve is arranged at the head end of the steam jacket pipe, the drain valve is communicated with the tail end of the steam jacket pipe, the steam pipe is communicated with the steam jacket pipe through the jacket heating valve and the heat insulation plug valve, and the other end of the drain valve is communicated with the condensate water recycling pipe. Oil content of waste water discharged by the slag discharging device is below 20mg/L and is smaller than waste water oil content index which is 50mg/L, so that the slag discharging device reduces working load of a gas floating oil removing machine in a biochemical system. The heat insulation plug valve and a heat insulation jacket are connected in series to use steam, so that secondary utilization of steam waste heat can be achieved.
Description
Technical field
The utility model relates to the high temperature slag discharging device of chemical plant, particularly a kind of ammonia still slag discharging device.
Background technology
Inhomogeneous and the latch up phenomenon of bed drain purge often appears in the ammonia still scum pipe of prior art.When scum pipe stops up, can only utilize to purify coal gas through burning the roasting deslagging that carries out.There is following deficiency in the deslagging of this mode: (1) deslagging complex procedures, and operation easier is big, and safety performance is low, and the input manpower is many, energy consumption is high, and production cost is high; When (2) scum pipe stops up with baked wheaten cake, use coal gas or gas welding that equipment is heated, influence service life of equipment, cause the ME rate to increase; (3) tower bear building-up slag row is unclean, in case discharge, slag-drip opening pitch slag splashes, and smell is big, serious law environment; (4) sometimes because of row does not slag tap, long-time barbecue, the dregs of fat in the pipe become dry gradually, need to stop production Residue extraction pipeline is cleared up; (5) distilled ammonia wastewater band oil is many, influences next procedure and normally moves.Therefore, demand developing that deslagging is unimpeded urgently, the ammonia still slag discharging device of environmental protection, safety.
Summary of the invention
For overcoming above-mentioned many deficiencies that prior art exists, the utility model provides a kind of ammonia still slag discharging device, and this device deslagging is unimpeded, environmental protection, safety.
The ammonia still slag discharging device of the utility model comprises ammonia still tower body, scum pipe, vapour pipe, steam-jacket pipe, water of condensation TFL, residual cake valve, steaming out valve, chuck heater valve, insulation stopcock and drain valve.Bottom at the ammonia still tower body is communicated with scum pipe, and scum pipe is provided with residual cake valve, on the scum pipe of residual cake valve bottom, is communicated with the steaming out valve; One end of steaming out valve is communicated with vapour pipe, and the end of scum pipe leads to slag bath, is provided with steam-jacket pipe at the skin of scum pipe; The head end of steam-jacket pipe is provided with the insulation stopcock; The terminal drain valve that is communicated with, vapour pipe is communicated with steam-jacket pipe through chuck heater valve and insulation stopcock, and the drain valve the other end is communicated with the water of condensation TFL.
The deslagging principle of the utility model: during deslagging, at first open chuck heater valve and insulation stopcock, make the steam in the vapour pipe get into steam-jacket pipe, regulate the insulation stopcock temperature of scum pipe is kept greater than 130 ℃; Next opens residual cake valve, and the dregs of fat are at high temperature discharged smoothly; At last, when deslagging finishes, open the steaming out valve, the dregs of fat in the scum pipe are swept totally, the water of condensation in the steam-jacket pipe gets into the water of condensation TFL through drain valve.
The beneficial effect of the utility model
The utility model is through being provided with steam-jacket pipe outside scum pipe; Steam in the vapour pipe is introduced steam-jacket pipe; The temperature of scum pipe is remained on more than 130 ℃, melt into rare shape in the scum pipe of the dregs of fat at the bottom of the tower under the steam jacket protection and flow in the slag bath, make deslagging not have dregs of fat latch up phenomenon; Remain unimpeded, the oil smoke that has produced when having eliminated deslagging simultaneously.The waste water oleaginousness of discharging through this device less than the standard of waste water band oil mass index 50mg/L, thereby has reduced the working load of biochemical system oil removal by air bubbling machine below 20mg/L.This device realizes need not special messenger's operation, and deslagging is evenly reliable, and the dregs of fat do not splash when discharging, and the smell that the dregs of fat produce is little, the deslagging cleaned in situ, and safety performance is high.This device adopts the insulation stopcock, and flexible operation is safe and reliable, utilizes insulation stopcock control bed drain purge.The insulation stopcock is connected with insulation jacket and is used steam, makes steam waste heat reach second stage employ.
Description of drawings
Fig. 1 is the structural representation of the utility model ammonia still slag discharging device.
Among the figure:
1,The ammonia still tower body, 2, scum pipe, 3, vapour pipe, 4, steam-jacket pipe, 5, the water of condensation TFL, 6, residual cake valve, 7, the steaming out valve, 8, the chuck heater valve, 9, the insulation stopcock, 10, drain valve.
Embodiment
Below in conjunction with accompanying drawing the utility model is further described.
A kind of ammonia still slag discharging device, as shown in Figure 1, comprise ammonia still tower body 1, scum pipe 2, vapour pipe 3, steam-jacket pipe 4, water of condensation TFL 5, residual cake valve 6, steaming out valve 7, chuck heater valve 8, insulation stopcock 9 and drain valve 10.Bottom at ammonia still tower body 1 is communicated with scum pipe 2; Scum pipe 2 is provided with residual cake valve 6, and the scum pipe 2 in residual cake valve 6 bottoms is communicated with steaming out valve 7, and an end of steaming out valve 7 is communicated with vapour pipe 3; The end of scum pipe 2 leads to slag bath; Skin at scum pipe 2 is provided with steam-jacket pipe 4, and the head end of steam-jacket pipe 4 is provided with insulation stopcock 9, the terminal drain valve 10 that is communicated with; Vapour pipe 3 is by chuck heater valve 8 connection of connect with insulation stopcock 9 and steam-jacket pipe 4, drain valve 10 the other ends connection water of condensation TFL 5.
During work, open chuck heater valve 8 and insulation stopcock 9, make the steam of vapour pipe 3 get into steam-jacket pipe 4; Open residual cake valve 6, regulate insulation stopcock 9 temperature of the dregs of fat in the scum pipe 3 is remained on more than 130 ℃, make the dregs of fat become scattered paste shape to flow to the deslagging pond smoothly; When deslagging finishes, open steaming out valve 7, the dregs of fat in the scum pipe 2 are purged clean; In entire work process, the water of condensation in the steam-jacket pipe 4 gets into water of condensation TFL 5 through drain valve 10.
Claims (1)
1. ammonia still slag discharging device; Comprise ammonia still tower body (1), scum pipe (2), vapour pipe (3), steam-jacket pipe (4), water of condensation TFL (5), residual cake valve (6), steaming out valve (7), chuck heater valve (8), insulation stopcock (9) and drain valve (10); It is characterized in that be communicated with scum pipe (2) in the bottom of ammonia still tower body (1), scum pipe (2) is provided with residual cake valve (6); Go up connection steaming out valve (7) at the scum pipe (2) of residual cake valve (6) bottom; One end of steaming out valve (7) is communicated with vapour pipe (3), and the end of scum pipe (2) leads to slag bath, is provided with steam-jacket pipe (4) at the skin of scum pipe (2); The head end of steam-jacket pipe (4) is provided with insulation stopcock (9); The terminal drain valve (10) that is communicated with, vapour pipe (3) is communicated with steam-jacket pipe (4) through chuck heater valve (8) and insulation stopcock (9), and drain valve (10) the other end is communicated with water of condensation TFL (5).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011203920322U CN202558653U (en) | 2011-10-16 | 2011-10-16 | Slag discharging device of ammonia still |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011203920322U CN202558653U (en) | 2011-10-16 | 2011-10-16 | Slag discharging device of ammonia still |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202558653U true CN202558653U (en) | 2012-11-28 |
Family
ID=47208333
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011203920322U Expired - Fee Related CN202558653U (en) | 2011-10-16 | 2011-10-16 | Slag discharging device of ammonia still |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202558653U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106630004A (en) * | 2016-11-17 | 2017-05-10 | 内蒙古大唐国际克什克腾煤制天然气有限责任公司 | Oil removal collection device for phenol and ammonia recycling system |
CN113318849A (en) * | 2021-06-09 | 2021-08-31 | 淄博英诺威圣节能科技有限公司 | Raw coal circulating screening and crushing device and screening and crushing method |
CN114853119A (en) * | 2022-06-21 | 2022-08-05 | 广东韶钢松山股份有限公司 | Ammonia still blowdown water treatment facilities and coal gas clean system |
CN115518515A (en) * | 2022-09-14 | 2022-12-27 | 山东莱钢永锋钢铁有限公司 | Coal-fired boiler denitration system improvement method |
-
2011
- 2011-10-16 CN CN2011203920322U patent/CN202558653U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106630004A (en) * | 2016-11-17 | 2017-05-10 | 内蒙古大唐国际克什克腾煤制天然气有限责任公司 | Oil removal collection device for phenol and ammonia recycling system |
CN113318849A (en) * | 2021-06-09 | 2021-08-31 | 淄博英诺威圣节能科技有限公司 | Raw coal circulating screening and crushing device and screening and crushing method |
CN114853119A (en) * | 2022-06-21 | 2022-08-05 | 广东韶钢松山股份有限公司 | Ammonia still blowdown water treatment facilities and coal gas clean system |
CN114853119B (en) * | 2022-06-21 | 2023-08-04 | 广东韶钢松山股份有限公司 | Ammonia still sewage treatment device and gas purification system |
CN115518515A (en) * | 2022-09-14 | 2022-12-27 | 山东莱钢永锋钢铁有限公司 | Coal-fired boiler denitration system improvement method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202558653U (en) | Slag discharging device of ammonia still | |
CN201954596U (en) | Oil and gas dual-purpose full-automatic civil kitchen range | |
CN204338011U (en) | Moisture film desulfuration spray tower | |
CN201746504U (en) | Improved coke dry quenching water sealing tank | |
CN101886878A (en) | Discharging method for tank-type calcining furnace | |
CN206996840U (en) | A kind of catalytic cracking flue gas processing structure | |
CN201028271Y (en) | Natural gas steam trap with drawer type filter | |
CN201973698U (en) | Flue gas waste heat recovery device | |
CN204007180U (en) | A kind of waste gas residual heat recycling and processing device | |
CN204880679U (en) | Energy -saving boiler of tape trailer gas disposal | |
CN204880726U (en) | Take condensation water treatment facilities's condensing gas heater | |
CN204484823U (en) | Edible fungi sterilization stove | |
CN210292882U (en) | Flue gas waste heat recovery device for silicon-chromium alloy electric furnace | |
CN203408704U (en) | Energy-saving, emission-reducing and consumption-reducing heating device for reaction kettle | |
CN201935230U (en) | Civil large cooking range | |
CN203700283U (en) | Devulcanizer for regeneration of onsite transformer oil desulfurizer | |
CN201882913U (en) | Tank type calcining furnace for preparing calcined petroleum coke | |
CN202192059U (en) | Hydraulic decoking system | |
CN204063605U (en) | One self-priming anti-water collecting device on oil field heating furnace | |
CN100551557C (en) | A kind of method of hot dipping cleaning scorch air pipe | |
CN207324420U (en) | A kind of fume treatment desulfurizing tower for preventing from blocking | |
CN202762298U (en) | Wet dust removal desulfurization device | |
CN205187909U (en) | Water treatment evaporator | |
CN205288077U (en) | Flue gas desulfurization ultra -clean discharging equipment | |
CN102788359A (en) | Smoke prevention and dust control-type boiler flue system |
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: 20121128 Termination date: 20181016 |