CN202508885U - Device for preparing hydrocyanic acid through oxygen enrichment - Google Patents
Device for preparing hydrocyanic acid through oxygen enrichment Download PDFInfo
- Publication number
- CN202508885U CN202508885U CN2012201737416U CN201220173741U CN202508885U CN 202508885 U CN202508885 U CN 202508885U CN 2012201737416 U CN2012201737416 U CN 2012201737416U CN 201220173741 U CN201220173741 U CN 201220173741U CN 202508885 U CN202508885 U CN 202508885U
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- ammonia
- natural gas
- tank
- bed filter
- oxygen enrichment
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Abstract
The utility model discloses a device for preparing hydrocyanic acid through oxygen enrichment, belonging to the technical field of preparation of hydrocyanic acid through oxygen enrichment. The device for preparing hydrocyanic acid through oxygen enrichment comprises a liquid ammonia storage tank, an evaporator, a heater, a buffer tank, an ammonia activated carbon adsorption tank, a bag ammonia filter, a mixer, a preheater, a quaternary gas mixer, a flame arrester and a hydrocyanic acid reactor, which are connected in sequence, wherein the mixer is also connected with a bag natural gas filter; the bag natural gas filter is connected with a natural gas activated carbon adsorption tank; the preheater is connected with a bag air filter; the bag air filter is connected with a pressure swing adsorber; and the quaternary gas mixer is also connected with a steam generator. The device has simple structure, is easy to operate, improves the production capacity and reduces the labor and production cost.
Description
Technical field
The utility model belongs to oxygen enrichment hydrogen manufacturing cyanic acid technical field, relates to a kind of device that is used for oxygen enrichment hydrogen manufacturing cyanic acid.
Background technology
The main method of producing prussic acid at present in the world has iS-One method, BMA method, Sha Wenni dry method, light oil cracking method etc.
IS-One method is a raw material with methane, ammonia and air, and platinum guaze is the synthetic prussic acid of catalyzer, but exists tail gas not recycle, and emptying is the shortcoming of contaminate environment again; The characteristics of BMA method are to make raw material with methane and ammonia, and platinum catalyst is distributed on the ceramic reaction tube, and raw material is through high-temperature catalytic reaction in the pipe; Reaction heat is supplied with by the outside; Heating temperature is up to 1400-1500 ℃, and the high temperature material of reactor drum is not easy to solve, and heat energy consumption is also very high; Light oil cracking method and Sha Wenni dry method are similar, are characterized in that with low-carbon alkanes such as ammonia and C1-C6 be raw material, adopt refinery coke (conductive particle) flowing bed reactor; Electrode is inserted in the thermopnore, and externally fed produces heat, keeps 1300～1600 ℃ of temperature of reaction; Electrisity consumption is very big; And the running period of its Reaktionsofen is short, and maintenance is frequent, and by product carbon is contaminate environment also.
In sum; In order to overcome the shortcoming of prior art; Researched and developed a kind of technology of oxygen enrichment legal system prussic acid; The air that is about to generally to use is at present done raw material and is changed oxygen-rich air into and do raw material, and oxygen-rich air can be joined air by making oxygen by air separation and produced, or carries gas behind the nitrogen by transformation absorption and allocate in the air and produce.Yet the device of existing hydrogen manufacturing cyanic acid all is not suitable for this technology.
Summary of the invention
The purpose of the utility model provides a kind of device that is used for oxygen enrichment hydrogen manufacturing cyanic acid.
The utility model is realized through following technical scheme:
A kind of device that is used for oxygen enrichment hydrogen manufacturing cyanic acid; Comprise the liquid ammonia storage tank, vaporizer, well heater, surge tank, ammonia absorbent charcoal adsorption tank, ammonia deep bed filter, mixing tank, preheater, quaternary gas mixer, spark arrester, the prussic acid reactor drum that connect successively; Wherein said mixing tank also is connected with the Sweet natural gas deep bed filter; The Sweet natural gas deep bed filter is connected with the Sweet natural gas absorbent charcoal adsorption tank; Described preheater also is connected with the air deep bed filter, and the air deep bed filter is connected with the transformation adsorber, and described quaternary gas mixer also is connected with vapour generator.
The liquefied ammonia that comes from liquid ammonia storage tank gets into the ammonia surge tank after getting into heater heats behind the liquefied ammonia vaporizer; The gas that comes out from the ammonia surge tank gets into the ammonia absorbent charcoal adsorption tank respectively and the ammonia deep bed filter carries out purifying treatment, and purified gas is sent into mixing tank; Getting into mixing tank after natural gas via Sweet natural gas absorbent charcoal adsorption tank and the Sweet natural gas deep bed filter purifying treatment mixes with the ammonia of purifying treatment; The incoming stock gas mixing of the gas preheater mixing preheating that the oxygen-rich air that comes from the transformation adsorber comes with mixing tank behind air pocket type filter cleaning; Gas mixture after the preheating gets into the quaternary gas mixer to be mixed with the steam that comes from vapour generator; Mixed quaternary gas gets into the prussic acid reactor drum at last through gas mixture deep bed filter, spark arrester, and tail gas send synthesis ammonia system.
The utility model is simple in structure, and easy handling has improved throughput, has reduced labour cost and production cost.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Among the figure: 1-liquid ammonia storage tank, 2-vaporizer, 3-well heater, 4-surge tank, 5-ammonia absorbent charcoal adsorption tank, 6-ammonia deep bed filter, 7-mixing tank, 8-preheater, 9-quaternary gas mixer, 10-spark arrester, 11-prussic acid reactor drum, 12-Sweet natural gas deep bed filter, 13-Sweet natural gas absorbent charcoal adsorption tank, 14-transformation adsorber, 15-air deep bed filter, 16-vapour generator.
Embodiment
Below in conjunction with accompanying drawing the utility model is further specified
A kind of device that is used for oxygen enrichment hydrogen manufacturing cyanic acid as shown in Figure 1; Comprise the liquid ammonia storage tank 1, vaporizer 2, well heater 3, surge tank 4, ammonia absorbent charcoal adsorption tank 5, ammonia deep bed filter 6, mixing tank 7, preheater 8, quaternary gas mixer 9, spark arrester 10, the prussic acid reactor drum 11 that connect successively; Wherein said mixing tank 7 also is connected with Sweet natural gas deep bed filter 12; Sweet natural gas deep bed filter 12 is connected with Sweet natural gas absorbent charcoal adsorption tank 13; Described preheater 8 also is connected with air deep bed filter 15, and air deep bed filter 15 is connected with transformation adsorber 14, and described quaternary gas mixer 9 also is connected with vapour generator 16.
Claims (1)
1. device that is used for oxygen enrichment hydrogen manufacturing cyanic acid; It is characterized in that comprising the liquid ammonia storage tank (1), vaporizer (2), well heater (3), surge tank (4), ammonia absorbent charcoal adsorption tank (5), ammonia deep bed filter (6), mixing tank (7), preheater (8), quaternary gas mixer (9), spark arrester (10), the prussic acid reactor drum (11) that connect successively; Wherein said mixing tank (7) also is connected with Sweet natural gas deep bed filter (12); Sweet natural gas deep bed filter (12) is connected with Sweet natural gas absorbent charcoal adsorption tank (13); Described preheater (8) also is connected with air deep bed filter (15); Air deep bed filter (15) is connected with transformation adsorber (14), and described quaternary gas mixer (9) also is connected with vapour generator (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012201737416U CN202508885U (en) | 2012-04-23 | 2012-04-23 | Device for preparing hydrocyanic acid through oxygen enrichment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012201737416U CN202508885U (en) | 2012-04-23 | 2012-04-23 | Device for preparing hydrocyanic acid through oxygen enrichment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202508885U true CN202508885U (en) | 2012-10-31 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012201737416U Expired - Fee Related CN202508885U (en) | 2012-04-23 | 2012-04-23 | Device for preparing hydrocyanic acid through oxygen enrichment |
Country Status (1)
| Country | Link |
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| CN (1) | CN202508885U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103539158A (en) * | 2013-10-25 | 2014-01-29 | 重庆紫光国际化工有限责任公司 | Production system and production method for synthesizing hydrocyanic acid by Andrussow process |
| CN103539159A (en) * | 2013-10-25 | 2014-01-29 | 重庆紫光国际化工有限责任公司 | Method for providing air for hydrocyanic acid production system and system thereof |
| US20180215626A1 (en) * | 2013-07-19 | 2018-08-02 | Arkema France | Installation and process for the preparation of hydrogen cyanide |
-
2012
- 2012-04-23 CN CN2012201737416U patent/CN202508885U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20180215626A1 (en) * | 2013-07-19 | 2018-08-02 | Arkema France | Installation and process for the preparation of hydrogen cyanide |
| US10865118B2 (en) * | 2013-07-19 | 2020-12-15 | Arkema France | Installation and process for the preparation of hydrogen cyanide |
| CN103539158A (en) * | 2013-10-25 | 2014-01-29 | 重庆紫光国际化工有限责任公司 | Production system and production method for synthesizing hydrocyanic acid by Andrussow process |
| CN103539159A (en) * | 2013-10-25 | 2014-01-29 | 重庆紫光国际化工有限责任公司 | Method for providing air for hydrocyanic acid production system and system thereof |
| CN103539158B (en) * | 2013-10-25 | 2016-02-03 | 重庆紫光国际化工有限责任公司 | The production system of iS-One method synthesis prussic acid and production method |
| CN103539159B (en) * | 2013-10-25 | 2016-05-04 | 重庆紫光国际化工有限责任公司 | For hydrogen cyanide production system provides method and the system thereof of air |
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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 |
Granted publication date: 20121031 Termination date: 20150423 |
|
| EXPY | Termination of patent right or utility model |