CN202415158U - Novel technical device for cleaner production of nitrogenous fertilizer system - Google Patents

Novel technical device for cleaner production of nitrogenous fertilizer system Download PDF

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Publication number
CN202415158U
CN202415158U CN2011205545321U CN201120554532U CN202415158U CN 202415158 U CN202415158 U CN 202415158U CN 2011205545321 U CN2011205545321 U CN 2011205545321U CN 201120554532 U CN201120554532 U CN 201120554532U CN 202415158 U CN202415158 U CN 202415158U
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CN
China
Prior art keywords
communicated
sulfur
tank
nitrogenous fertilizer
pressure filter
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
CN2011205545321U
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Chinese (zh)
Inventor
孟兆武
尚秀兰
张海杰
王娟
杨泽银
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.)
SHANDONG ACID CHEMICALS CO Ltd
Original Assignee
SHANDONG ACID CHEMICALS 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 SHANDONG ACID CHEMICALS CO Ltd filed Critical SHANDONG ACID CHEMICALS CO Ltd
Priority to CN2011205545321U priority Critical patent/CN202415158U/en
Application granted granted Critical
Publication of CN202415158U publication Critical patent/CN202415158U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model provides a novel technical device for cleaner production of a nitrogenous fertilizer system. The novel technical device comprises a regeneration tank (1), a foam tank (2), a pump body (3), a press filter (4), a sulfur melting kettle (5) and a barren liquor tank (6), wherein the regeneration tank (1) is arranged to be communicated with the foam tank (2); the press filter (4) is arranged to be communicated with the foam tank (2) by the pump body (3); and the output end of the press filter (4) is arranged in such a way that one path of the output end is communicated with the sulfur melting kettle (5) while the other path of the output end is communicated with the barren liquor tank (6). Therefore, the sulfur recycling efficiency and the sulfur removing effect are improved, and the discharge of ammonia and sulfur contained foam waste water of a sulfur removing system is eliminated.

Description

Nitrogenous fertilizer system cleaner production new technology device
One, technical field
The utility model relates to nitrogenous fertilizer system cleaner production new technology, a kind of nitrogenous fertilizer system cleaner production new technology device, and especially a kind of adaptation is used for the sulfur recovery facility in the coal gas desulfurization system of nitrogen fertilizer production.
Two, background technology
In nitrogen fertilizer production, use coal gas as a kind of raw material usually, when using coal gas; Need carry out desulfurization to coal gas handles and recovery sulier; Therefore sulfur recovery facility is an important chemical equipment, in existing nitrogenous fertilizer system cleaner production new technology device, because the suspension sulphur in the doctor solution and reduce the side reaction that causes because of the sulfur melting kettle heating; Desulfurization is produced adverse influence, thereby influence the sweetening effectiveness of coal gas.
Three, summary of the invention
In order to overcome above-mentioned technical disadvantages, the purpose of the utility model provides a kind of nitrogenous fertilizer system cleaner production new technology device, has therefore improved the efficient of recovery sulier and the effect of desulfurization, has stopped the discharging that desulphurization system contains ammonia, sulfur-bearing foam waste water.
For achieving the above object; The technical scheme that the utility model is taked is: include regeneration tank, foam chute, the pump housing, pressure filter, sulfur melting kettle and lean solution groove; Regeneration tank is set to be communicated with foam chute; Pressure filter is set to be communicated with foam chute through the pump housing, and the output terminal of pressure filter is set to one the tunnel be communicated with sulfur melting kettle, another road is set to is communicated with the lean solution groove.
The doctor solution that coal gas is carried out after the desulfurization enters into regeneration tank, through the foam chute and the pump housing, is pressed in the sulfur melting kettle by pressure filter; In sulfur melting kettle, sulphur is reclaimed; Owing to designed pressure filter, improved the pressure that gets into the doctor solution of sulfur melting kettle, the doctor solution speed of circulation is improved; Therefore improve the efficient of recovery sulier and the effect of desulfurization, stopped the discharging that desulphurization system contains ammonia, sulfur-bearing foam waste water.
The utility model has designed, and pressure filter is set to plate and frame(type)filter press.
Four, description of drawings
Accompanying drawing 1 is the synoptic diagram of the utility model.
Five, embodiment
Accompanying drawing is an embodiment of the utility model; Specify present embodiment in conjunction with accompanying drawing; Include regeneration tank 1, foam chute 2, the pump housing 3, pressure filter 4, sulfur melting kettle 5 and lean solution groove 6; Regeneration tank 1 is set to be communicated with foam chute 2, and pressure filter 4 is set to be communicated with foam chute 2 through the pump housing 3, and the output terminal of pressure filter 4 is set to one the tunnel be communicated with sulfur melting kettle 5, another road is set to is communicated with lean solution groove 6.
In the present embodiment, pressure filter 4 is set to plate and frame(type)filter press.
The doctor solution that coal gas is carried out after the desulfurization enters into regeneration tank 1, through the foam chute 2 and the pump housing 3, is pressed in the sulfur melting kettle 5 by pressure filter 4, in sulfur melting kettle 5, sulphur is reclaimed.
The characteristics of the utlity model has down:
1, owing to designed pressure filter 4, improved the pressure that gets into the doctor solution of sulfur melting kettle 5, the doctor solution speed of circulation is improved, therefore improved the efficient of recovery sulier and the effect of desulfurization.
2, molten sulphur raffinate quantity discharged every day was not before the desulphurization system sulphur recovery was done and transformed: 60m 3, transforming back residual liquid discharge amount is 6m 3/ day.Sulfur recovery rate is brought up to more than 85% by 70 original %, for tar content, raising gas sweetening quality and the desulfuration efficiency, the reduction that reduce in the semi-water gas influence of descending operation, the trend of slowing down the rising of thionizer pressure reduction is played positive effect.
In nitrogenous fertilizer system cleaner production new technology device technique field; Every regeneration tank 1 that includes is set to be communicated with foam chute 2; Pressure filter 4 is set to be communicated with foam chute 2 through the pump housing 3, and the technology contents that the output terminal of pressure filter 4 is set to a tunnel to be communicated with sulfur melting kettle 5, another road is set to be communicated with lean solution groove 6 is all in the protection domain of the utility model.

Claims (2)

1. nitrogenous fertilizer system cleaner production new technology device; It is characterized in that: include regeneration tank (1), foam chute (2), the pump housing (3), pressure filter (4), sulfur melting kettle (5) and lean solution groove (6); Regeneration tank (1) is set to be communicated with foam chute (2); Pressure filter (4) is set to be communicated with foam chute (2) through the pump housing (3), and the output terminal of pressure filter (4) is set to one the tunnel be communicated with sulfur melting kettle (5), another road is set to is communicated with lean solution groove (6).
2. nitrogenous fertilizer according to claim 1 system cleaner production new technology device; It is characterized in that: pressure filter (4) is set to plate and frame(type)filter press.
CN2011205545321U 2011-12-27 2011-12-27 Novel technical device for cleaner production of nitrogenous fertilizer system Expired - Fee Related CN202415158U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011205545321U CN202415158U (en) 2011-12-27 2011-12-27 Novel technical device for cleaner production of nitrogenous fertilizer system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011205545321U CN202415158U (en) 2011-12-27 2011-12-27 Novel technical device for cleaner production of nitrogenous fertilizer system

Publications (1)

Publication Number Publication Date
CN202415158U true CN202415158U (en) 2012-09-05

Family

ID=46739941

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011205545321U Expired - Fee Related CN202415158U (en) 2011-12-27 2011-12-27 Novel technical device for cleaner production of nitrogenous fertilizer system

Country Status (1)

Country Link
CN (1) CN202415158U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105709475A (en) * 2016-04-15 2016-06-29 贵阳铝镁设计研究院有限公司 Coal gas desulfuration barren solution quality and effectiveness improving system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105709475A (en) * 2016-04-15 2016-06-29 贵阳铝镁设计研究院有限公司 Coal gas desulfuration barren solution quality and effectiveness improving system

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120905

Termination date: 20131227