CN203108233U - Self-evaporation structure for deposited liquid ammonia in gas ammonia delivery pipe - Google Patents
Self-evaporation structure for deposited liquid ammonia in gas ammonia delivery pipe Download PDFInfo
- Publication number
- CN203108233U CN203108233U CN 201320066452 CN201320066452U CN203108233U CN 203108233 U CN203108233 U CN 203108233U CN 201320066452 CN201320066452 CN 201320066452 CN 201320066452 U CN201320066452 U CN 201320066452U CN 203108233 U CN203108233 U CN 203108233U
- Authority
- CN
- China
- Prior art keywords
- ammonia
- gas
- carrier pipe
- gas ammonia
- liquefied ammonia
- 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
Links
Images
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
The utility model discloses a self-evaporation structure for deposited liquid ammonia in a gas ammonia delivery pipe. The self-evaporation structure comprises the gas ammonia delivery pipe (1), wherein a liquid ammonia deposition pipe (2) is arranged at the bottom of the gas ammonia delivery pipe (1); and a heating device (3) is arranged outside the liquid ammonia deposition pipe (2). Deposited liquid ammonia in the gas ammonia delivery pipe is collected in the pipe, heated to evaporate into gas ammonia, and enters the gas ammonia delivery pipe to participate in a working cycle or be recycled. The liquid ammonia automatically flows into the liquid ammonia deposition pipe by virtue of flowability of liquid, additional equipment is not needed, the liquid ammonia can be evaporated so long as the heating device is started, the whole operation process is simple and feasible, the equipment cost is low, and the using effect is good.
Description
Technical field
The utility model relates to gas ammonia conveying technology field, deposition liquefied ammonia spontaneous evaporation structure in especially a kind of gas ammonia carrier pipe.
Background technology
At present, in production of synthetic ammonia, liquefied ammonia is realized the cool cycles utilization as evaporation, compression and the liquefaction that cooling medium passes through repeatedly.But in process of production, the gas ammonia carrier pipe may be brought liquefied ammonia into because of abnormal operation, and deposition appears in liquefied ammonia in the gas ammonia carrier pipe, can damage pipe support by pressure when serious, causes pipeline to damage.And if the liquefied ammonia that has deposited do not establish is led pouring and then is difficult to derive, and going wrong is difficult for maintenance, is difficult for displacement, brings difficulty for processing subsequently.The method of the liquefied ammonia that deposits in handling the gas ammonia carrier pipe is at present, leads pouring in the low spot setting of gas ammonia carrier pipe, the discharging of guiding liquefied ammonia.But such method need add pumping installations, causes safety place but also will set up the longer pipe road.So not only increased equipment investment, and complex operation, effect is also undesirable simultaneously.
Summary of the invention
The purpose of this utility model is: deposition liquefied ammonia spontaneous evaporation structure in a kind of gas ammonia carrier pipe is provided, and it can effectively solve the problem of deposition liquefied ammonia in the gas ammonia carrier pipe, and simple in structure, equipment drops into low, easy and simple to handle, treatment effect is good, to overcome the deficiencies in the prior art.
The utility model is achieved in that deposition liquefied ammonia spontaneous evaporation structure in the gas ammonia carrier pipe, comprises the gas ammonia carrier pipe, is provided with the liquefied ammonia deposited tube in the bottom of gas ammonia carrier pipe, is provided with heater in liquefied ammonia deposited tube outside.
Be connected with the gas ammonia recovery tube at the gas ammonia carrier pipe.Generally, the liquefied ammonia of evaporation can enter in the production cycle, still, makes at the liquefied ammonia that is in end-of-life state and need to handle deposition, and the liquefied ammonia of evaporation can enter ammonia recovery unit by the gas ammonia recovery tube.
The liquefied ammonia deposited tube is more than one.According to the laying condition of pipeline, easily on the position of deposition liquefied ammonia corresponding liquefied ammonia deposited tube is set at each, can avoid that so also all liquefied ammonia are concentrated on the pipeline minimum point and evaporate and cause the situation that evaporation capacity may deficiency.
Be provided with fluid level indicator at the liquefied ammonia deposited tube.
Described heater is jacket type or coiled, or electrical heating type.The thermal source of jacket type or coiled can adopt steam.
Heater is the steam coil pipe, and the one end is the steam inlet, and the other end is condensate outlet, is provided with steam trap at condensate outlet.
Owing to adopted technique scheme, compared with prior art, the utility model converges the liquefied ammonia that deposits in the gas ammonia carrier pipe in pipeline, makes liquefied ammonia be evaporated to gas ammonia by heating then, enter again in the gas ammonia carrier pipe and participate in working cycles, or reclaim.The utility model utilizes the self drainage of liquid that liquefied ammonia is flowed in the liquefied ammonia deposited tube voluntarily, need not to use extra equipment, only needs to start heater and can make the liquefied ammonia evaporation, and the whole operation process is simple, and equipment cost is low, and result of use is good.The utility model is simple in structure, makes easily, and with low cost, result of use is good.
Description of drawings
Accompanying drawing 1 is structural representation of the present utility model.
The specific embodiment
Embodiment of the present utility model: deposition liquefied ammonia spontaneous evaporation structure as shown in Figure 1 in the gas ammonia carrier pipe, comprise gas ammonia carrier pipe 1, the number position that is provided with liquefied ammonia deposited tube 2(liquefied ammonia deposited tube 2 in the bottom of gas ammonia carrier pipe 1 is decided according to the arrangement mode of gas ammonia carrier pipe 1), be provided with heater 3 in liquefied ammonia deposited tube 2 outsides, heater 3 adopts steam coil pipe (also can adopt the electrical heating coil pipe as required), one end of steam coil pipe is steam inlet 8, steam inlet 8 is connected on the source of water vapor, the other end of steam coil pipe is condensate outlet 7, be provided with steam trap 9 at condensate outlet 7, be provided with fluid level indicator 5 at liquefied ammonia deposited tube 2, be connected with gas ammonia recovery tube 4 at gas ammonia carrier pipe 1.
Claims (6)
1. deposit liquefied ammonia spontaneous evaporation structure in a gas ammonia carrier pipe, comprise gas ammonia carrier pipe (1), it is characterized in that: be provided with liquefied ammonia deposited tube (2) in the bottom of gas ammonia carrier pipe (1), be provided with heater (3) in liquefied ammonia deposited tube (2) outside.
2. deposition liquefied ammonia spontaneous evaporation structure in the gas ammonia carrier pipe according to claim 1 is characterized in that: be connected with gas ammonia recovery tube (4) at gas ammonia carrier pipe (1).
3. deposit liquefied ammonia spontaneous evaporation structure in the gas ammonia carrier pipe according to claim 1 and 2, it is characterized in that: liquefied ammonia deposited tube (2) is more than one.
4. deposition liquefied ammonia spontaneous evaporation structure in the gas ammonia carrier pipe according to claim 3 is characterized in that: be provided with fluid level indicator (5) at liquefied ammonia deposited tube (2).
5. deposit liquefied ammonia spontaneous evaporation structure in the gas ammonia carrier pipe according to claim 1, it is characterized in that: described heater (3) is jacket type or coiled, or electrical heating type.
6. deposit liquefied ammonia spontaneous evaporation structure in the gas ammonia carrier pipe according to claim 1 or 5, it is characterized in that: heater (3) is the steam coil pipe, the one end is steam inlet (8), and the other end is condensate outlet (7), is provided with steam trap (9) at condensate outlet (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320066452 CN203108233U (en) | 2013-02-05 | 2013-02-05 | Self-evaporation structure for deposited liquid ammonia in gas ammonia delivery pipe |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320066452 CN203108233U (en) | 2013-02-05 | 2013-02-05 | Self-evaporation structure for deposited liquid ammonia in gas ammonia delivery pipe |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203108233U true CN203108233U (en) | 2013-08-07 |
Family
ID=48888613
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320066452 Expired - Lifetime CN203108233U (en) | 2013-02-05 | 2013-02-05 | Self-evaporation structure for deposited liquid ammonia in gas ammonia delivery pipe |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203108233U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103083927A (en) * | 2013-02-05 | 2013-05-08 | 贵州开阳化工有限公司 | Spontaneous evaporation method for depositing liquefied ammonia in gas ammonia convey tube, and structure thereof |
-
2013
- 2013-02-05 CN CN 201320066452 patent/CN203108233U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103083927A (en) * | 2013-02-05 | 2013-05-08 | 贵州开阳化工有限公司 | Spontaneous evaporation method for depositing liquefied ammonia in gas ammonia convey tube, and structure thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203108233U (en) | Self-evaporation structure for deposited liquid ammonia in gas ammonia delivery pipe | |
| CN203657532U (en) | Energy-saving heat exchange device | |
| CN104266175A (en) | Superheating boiler superheating steam desalting device for oil field steam injection and utilization method thereof | |
| CN203429426U (en) | Condensed water recovery system for dyeing and finishing process | |
| CN202844602U (en) | Microwave-heating device for waste acid regeneration | |
| CN202762414U (en) | Glycol regenerating device | |
| CN103083927A (en) | Spontaneous evaporation method for depositing liquefied ammonia in gas ammonia convey tube, and structure thereof | |
| CN104329830A (en) | Turbine dead steam waste heat recovery process method | |
| CN204254928U (en) | A kind of turbine exhaust steam waste heat recycling device | |
| CN203517756U (en) | Steam recycling system of reeling machine | |
| CN203469500U (en) | Evaporator for petroleum and natural gas medium-and-low-grade waste heat power generation | |
| CN202881133U (en) | Device for direct supplying methyl chloride to chlorination reaction | |
| CN203010574U (en) | Cooling device for cooling condensation water at inlet of condensation pump | |
| CN202844605U (en) | Temperature-controllable split type liquid ammonia evaporator | |
| CN207113328U (en) | A kind of direct-evaporating type ice pulp grinder group | |
| CN205155903U (en) | A steam generator for producing injection water | |
| CN204125169U (en) | Improve the device of steam utilization in Phosphoric Acid Concentration process | |
| CN217843813U (en) | Acetone device low pressure lime set recovery system | |
| CN202647696U (en) | Off-machine coater heat supply recycling operation system | |
| CN204648198U (en) | Recycling of condensed steam system | |
| CN205227915U (en) | Solar energy sprays cold hot water system | |
| CN204281641U (en) | Heat pump ethylene recovery system | |
| CN203223909U (en) | Steam condensation water airtight recovery device | |
| CN204404163U (en) | A kind of Low Temperature Steam reclaimer | |
| CN203699950U (en) | Efficient self-cooling water distiller |
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: 20160311 Address after: 273500 Shandong city of Jining province Fushan Road No. 298 Patentee after: YANKUANG GROUP Co.,Ltd. Address before: Guizhou province Guiyang City Kaiyang County 550306 Yong Wen Xiang Huang Bai wells Patentee before: GUIZHOU KAIYANG CHEMICAL Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130807 |