CN201322437Y - Ammonia waste water heating furnace - Google Patents

Ammonia waste water heating furnace Download PDF

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Publication number
CN201322437Y
CN201322437Y CNU2008202243084U CN200820224308U CN201322437Y CN 201322437 Y CN201322437 Y CN 201322437Y CN U2008202243084 U CNU2008202243084 U CN U2008202243084U CN 200820224308 U CN200820224308 U CN 200820224308U CN 201322437 Y CN201322437 Y CN 201322437Y
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CN
China
Prior art keywords
heating furnace
waste water
ammonia
furnace body
water
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
CNU2008202243084U
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Chinese (zh)
Inventor
姜爱国
张友棣
王光华
梁玉河
李清田
王登富
赵杰
陈善龙
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.)
Jinan Metallurgical & Chemical Equipment Co Ltd
Original Assignee
Jinan Metallurgical & Chemical Equipment Co Ltd
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Publication date
Application filed by Jinan Metallurgical & Chemical Equipment Co Ltd filed Critical Jinan Metallurgical & Chemical Equipment Co Ltd
Priority to CNU2008202243084U priority Critical patent/CN201322437Y/en
Application granted granted Critical
Publication of CN201322437Y publication Critical patent/CN201322437Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • 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

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

The utility model discloses an ammonia waste water heating furnace which belongs to the coking equipment, in particular to a supporting device of ammonia-distill tower. The ammonia waste water heating furnace comprises a heating furnace body, furnace legs, a combustor and a chimney, and is characterized in that a heating furnace tube is arranged inside the heating furnace body; the bottom part of the furnace body is provided with the combustor; the top part of the heating furnace body is provided with a waste water pre-heater; the upper part of the pre-heater is provided with a smoke gas surplus heat recycler; a pre-heating water outlet of the waste water pre-heater is connected with a heating water inlet, and the hot air outlet of the surplus heat recycler is connected with an air outlet of the combustor on the bottom part of the furnace body. The utility model provides an ammonia waste water heating device; coke-oven gas is utilized to heat the ammonia waste water to an over-heated status, and then the ammonia waste water is sent into the tower, so that the over-heated water is changed to be steam at the moment entering the tower so as to steam the ammonia, and the condensed water is recycled to the heating furnace to heat. With the ammonia waste water heating furnace, external steam can be saved, and partial ammonia waste water is utilized, so that the waste water discharging quantity can be reduced, thereby saving energy and protecting the environment.

Description

The distilled ammonia wastewater heating furnace
Technical field
The utility model belongs to coker, particularly the corollary equipment of ammonia still.
Background technology
Can produce a large amount of ammonia-containing waters in the coking industry production process, waste water does not allow to efflux because of containing the ammonia event, and ammonia-containing water is serious to metal erosion, so must discharge after the ammonia extraction again.Traditional method is that waste water is sent in the ammonia still, distills with a large amount of steam, and ammonia is extracted.This method is used steam expense height, and pressure transient, and steam condensate (SC) mixes wastewater flow rate is strengthened simultaneously, so this technology falls behind, efficient is low, energy consumption is high, pollution is big.
The utility model content
Use steam distillation to carry ammonia in order to overcome existing ammonia still, the deficiency of energy consumption height, increase wastewater flow rate, the purpose of this utility model provides a kind of distilled ammonia wastewater heating furnace, and this distilled ammonia wastewater heating furnace is thermal efficiency height not only, and can not increase the quantity of ammonia-containing water.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of distilled ammonia wastewater heating furnace, comprise heating furnace body, stove leg, burner, chimney, it is characterized in that: furnace tubing is housed in the heating furnace body, bottom of furnace body is equipped with burner, the waste water preheater is equipped with at the heating furnace body top, preheater top is the flue gas waste heat recovery device, and the preheating water outlet of waste water preheater connects and adds the hot water inlet, and the waste-heat recoverer hot-blast outlet connects the air intlet of bottom of furnace body burner.
Described furnace tubing be spiral coil its add hot water outlet and be connected with ammonia still.
The preheating water inlet that described waste water preheater is finned coiled pipe preheater is connecting the ammonia still wastewater outlet.
Described flue gas waste heat recovery device is the heat pipe-type waste-heat recovery device.
The utility model provides a kind of ammonia still waste water firing equipment, utilizes coke-stove gas that distilled ammonia wastewater is heated to superheat state, carries in tower then, and superheated water is gone into tower and promptly become water vapour and carry out ammonia still process, and condensed water returns heating furnace circulation heating again.Using this equipment can save external steam, utilized the part distilled ammonia wastewater can reduce wastewater discharge simultaneously, is a kind of new equipment of energy-saving and environmental protection.
Description of drawings
Accompanying drawing 1 is a structural representation of the present utility model,
Among the figure, 1. cold wind import, 2. waste-heat recoverer, 3. waste water preheater, 4. the preheating water inlet 5. adds hot water outlet, 6. heating furnace body, 7. furnace tubing, 8. burner, 9. the stove leg 10. adds the hot water inlet, the outlet of 11. preheating water, 12. hot-blast outlets, 13. chimneys.
The specific embodiment
The specific embodiment of the present utility model is, as shown in the figure:
Embodiment 1, a kind of distilled ammonia wastewater heating furnace, comprise heating furnace body 6, stove leg 9, burner 8, chimney 13, it is characterized in that: furnace tubing 7 is housed in the heating furnace body, bottom of furnace body is equipped with burner, and waste water preheater 3 is equipped with at the heating furnace body top, and preheater top is flue gas waste heat recovery device 2, the preheating water outlet 11 of waste water preheater connects and adds hot water inlet 10, and waste-heat recoverer hot-blast outlet 12 connects the air intlet of bottom of furnace body burner.Described furnace tubing is a spiral coil, and it adds hot water outlet 5 and is connected with ammonia still.Described waste water preheater is finned coiled pipe preheater, and preheating water inlet 4 is connecting the ammonia still wastewater outlet.Described flue gas waste heat recovery device is the heat pipe-type waste-heat recovery device, and the self cooling wind inlet 1 of air enters waste-heat recovery device.
Waste water from ammonia still enters waste water preheater 3 by water pump through preheating water inlet 4, come out to enter heating furnace 6 by outlet 11 after the preheating, be heated to more than 120 degree, flow out by outlet 5 by adding hot water inlet 10, reached superheat state, can enter ammonia still according to the amount of technological requirement; Tank in the middle of condensed water after the heat release falls at the bottom of the tower is drawn back into stove by water pump then and is circulated.The waste water preheater has adopted advanced finned tube to carry out heat exchange, to improve the thermal efficiency.Through heat pipe-type waste-heat recoverer 2, the waste heat after the recovery can be heated to the 100-150 degree to cold air and send into burner 8 again before the stove flue gas was overflowed.But energy savings but also can improve efficiency of combustion greatly not only.

Claims (4)

1. distilled ammonia wastewater heating furnace, comprise heating furnace body, stove leg, burner, chimney, it is characterized in that: furnace tubing is housed in the heating furnace body, bottom of furnace body is equipped with burner, the waste water preheater is equipped with at the heating furnace body top, preheater top is the flue gas waste heat recovery device, and the preheating water outlet of waste water preheater connects and adds the hot water inlet, and the waste-heat recoverer hot-blast outlet connects the air intlet of bottom of furnace body burner.
2. distilled ammonia wastewater heating furnace according to claim 1 is characterized in that: described furnace tubing is a spiral coil.
3. distilled ammonia wastewater heating furnace according to claim 1 is characterized in that: described waste water preheater is finned coiled pipe preheater.
4. distilled ammonia wastewater heating furnace according to claim 1 is characterized in that: described flue gas waste heat recovery device is the heat pipe-type waste-heat recovery device.
CNU2008202243084U 2008-11-27 2008-11-27 Ammonia waste water heating furnace Expired - Lifetime CN201322437Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008202243084U CN201322437Y (en) 2008-11-27 2008-11-27 Ammonia waste water heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008202243084U CN201322437Y (en) 2008-11-27 2008-11-27 Ammonia waste water heating furnace

Publications (1)

Publication Number Publication Date
CN201322437Y true CN201322437Y (en) 2009-10-07

Family

ID=41159818

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008202243084U Expired - Lifetime CN201322437Y (en) 2008-11-27 2008-11-27 Ammonia waste water heating furnace

Country Status (1)

Country Link
CN (1) CN201322437Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104083883A (en) * 2014-07-15 2014-10-08 天津市奥利达燃气设备技术有限公司 Steam secondary-cooling-type liquid ammonia evaporator
CN108917175A (en) * 2018-07-17 2018-11-30 海宁市英德赛电子有限公司 A kind of high-purity ammon tank car heating system and its heating means
CN112299513A (en) * 2020-11-06 2021-02-02 内蒙古万众炜业科技环保股份公司 Ammonia distillation and dephenolization coupling device and process for wastewater for semi-coke production

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104083883A (en) * 2014-07-15 2014-10-08 天津市奥利达燃气设备技术有限公司 Steam secondary-cooling-type liquid ammonia evaporator
CN108917175A (en) * 2018-07-17 2018-11-30 海宁市英德赛电子有限公司 A kind of high-purity ammon tank car heating system and its heating means
CN112299513A (en) * 2020-11-06 2021-02-02 内蒙古万众炜业科技环保股份公司 Ammonia distillation and dephenolization coupling device and process for wastewater for semi-coke production

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Granted publication date: 20091007