CN2873784Y - Industrial gas phenolic liquid evaporator - Google Patents
Industrial gas phenolic liquid evaporator Download PDFInfo
- Publication number
- CN2873784Y CN2873784Y CN 200620080218 CN200620080218U CN2873784Y CN 2873784 Y CN2873784 Y CN 2873784Y CN 200620080218 CN200620080218 CN 200620080218 CN 200620080218 U CN200620080218 U CN 200620080218U CN 2873784 Y CN2873784 Y CN 2873784Y
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- gas
- phenol
- heating chamber
- industrial gas
- industrial
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Abstract
Disclosed is an industrial gas phenol liquid evaporator relating to industrial gas stove phenol liquid acid processing device field. The industrial gas phenol liquid evaporator comprises a shell, a gas inlet and a gas outlet, and is characterized in that the gas inlet (1) is connected to a vapor chamber (2), the vapor chamber (2) is connected to a heating chamber (5), an upper tube plate (4) is arranged on the end of the heating chamber (5), a lower tube plate (7) is arranged on the bottom of the heating chamber, a hole is punched in the upper plate (4) and lower tube plate (7), a gas tube array (5) is arranged in the hole of the upper plate (4) and lower tube plate (7). The industrial gas phenol liquid evaporator has the advantages of simple structure and saving energy or the like. With the industrial gas phenol liquid evaporator, the waste liquid of phenol water which is produced by the industrial gas stove can be circularly reused, and the question of the phenol water pollution of staticizing gas which perplexes people is thoroughly solved and a gap in this field is supplied.
Description
Technical field
Industrial gas phenol liquid vaporizer belongs to industrial gas furnace phenol liquid processing device field.
Background technology
At present, in industrial gas is produced, in order to obtain clean coal gas, often the thick heating gas that gas furnace is produced cools off scrubbing dust collection, will use a large amount of recirculated water that coal gas is directly washed like this, water to contain the phenol amount more and more higher, heating gas contains certain saturation moisture, make phenol water more and more higher, the discharging meeting causes severe contamination to environment.
The utility model content
Technical problem to be solved in the utility model is: overcome the problem that prior art exists, the industrial gas phenol liquid vaporizer of a kind of simple in structure, phenol water rate liquid recycle that the industrial gas stove can be produced, protection environment, save energy is provided.
In order to solve the problems of the technologies described above, the technical scheme that the utility model adopted is: this industrial gas phenol liquid vaporizer, comprise housing, gas inlet, gas exit, it is characterized in that: gas inlet links to each other with sweating room, sweating room links to each other with heating chamber, and the heating chamber end is provided with upper tubesheet, and the bottom is provided with lower tubesheet, have the hole on the last lower tubesheet, the coal gas tubulation is installed in the hole of lower tubesheet.
The sweating room both sides are provided with chuck, and chuck communicates with heating chamber, and chuck top one side is provided with vapour outlet, discharge of phenolic water mouth, and opposite side is provided with water level interface.
Heating chamber divides two bodies, and the upper body diameter is greater than lower body, and a side is provided with safe water and seals.Tube sheet top, heating chamber lower body bottom one side is provided with phenol water inlet and clean-up port, and the lower tubesheet below is a cavity, and cavity one side links to each other with gas exit.
Compared with prior art, the beneficial effect that the utility model had is: simple in structure, and the phenol water rate liquid recycle that the industrial gas stove can be produced.This industrial gas phenol liquid vaporizer is installed on the air cooler of producer gas generator, thick heating gas is entered by gas inlet, at first contact after entering heat exchange takes place with the sweating room inwall, coal gas enters tubulation and flows out through gas exit then, the outside of tubulation contacts with phenol water, phenol water absorption portion heat energy, reach boiling and produce steam by normal temperature, part phenol liquid thereupon by liquid state become gaseous state with vapor mixing to, this part mixed gas arrives the gas furnace bottom through vapour outlet by pipe-line transportation, enter the producer gas generator fire bed, harmful part incinerates through fire bed, and vapor portion satisfies system gas (because of the vaporization agent of production course of gas is a steam).The protection environment has been saved the energy again.Thoroughly solve the phenol water pollution problems that calmization system gas perplexs everybody, filled up the blank in this area.
Description of drawings
Fig. 1 is the structural representation of the utility model embodiment.
Wherein: 1 gas inlet, 2 sweating rooms, 3 water level interfaces, 4 upper tubesheets, 5 tubulations, 6 heating chambers, 7 lower tubesheets, 8 gas exits, 9 clean-up ports, 10 phenol water inlets, 11 safe waters seal 12 phenol slurry discharge outlet, 13 vapour outlets.
Embodiment
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail:
As shown in Figure 1, this industrial gas phenol liquid vaporizer, by gas inlet 1, sweating room 2, water level interface 3, upper tubesheet 4, tubulation 5, heating chamber 6, lower tubesheet 7, gas exit 8, clean-up port 9, phenol water inlet 10, safe water seal 11, phenol slurry discharge outlet 12, vapour outlet 13 form.One-piece construction is circular.Sweating room 2 links to each other with heating chamber 5, and heating chamber 5 ends are provided with upper tubesheet 4, and the bottom is provided with lower tubesheet 7, has the hole on the last lower tubesheet 4,7, and coal gas tubulation 5 is installed in the hole of lower tubesheet 4,7.Sweating room 2 links to each other with gas inlet 1, and sweating room 2 both sides are provided with chuck, and chuck communicates with heating chamber 5, and chuck top one side is provided with vapour outlet 13, discharge of phenolic water mouth 12, and opposite side is provided with a plurality of water level interfaces 3.6 minutes two bodies of heating chamber, the upper body diameter is greater than lower body, and a side is provided with safe water and seals 11.Tube sheet 7 tops, heating chamber 6 lower bodies bottom one side is provided with phenol water inlet 10 and clean-up port 9, and lower tubesheet 7 belows are a cavity, and cavity one side links to each other with gas exit 8.
Principle of work and working process are: this industrial gas phenol liquid vaporizer is installed on the air cooler of producer gas generator, thick heating gas is entered by gas inlet 1, at first contact after entering heat exchange takes place with sweating room 2 inwalls, coal gas enters tubulation 5 through gas exit 8 outflows then, the outside of tubulation 5 contacts with phenol water, phenol water absorption portion heat energy, reach boiling and produce steam by normal temperature, part phenol liquid thereupon by liquid state become gaseous state with vapor mixing to, this part mixed gas arrives the gas furnace bottom through vapour outlet 13 by pipe-line transportation, enter the producer gas generator fire bed, harmful part incinerates through fire bed, and vapor portion satisfies system gas.
Claims (4)
1, industrial gas phenol liquid vaporizer, comprise housing, gas inlet, gas exit, it is characterized in that: gas inlet (1) links to each other with sweating room (2), sweating room (2) links to each other with heating chamber (5), heating chamber (5) end is provided with upper tubesheet (4), the bottom is provided with lower tubesheet (7), has the hole on last lower tubesheet (4), (7), and coal gas tubulation (5) is installed in the hole of lower tubesheet (4), (7).
2, industrial gas phenol liquid vaporizer according to claim 1 is characterized in that: heating chamber (6) divides two bodies, and the upper body diameter is greater than lower body, and a side is provided with safe water and seals (11).
3, industrial gas phenol liquid vaporizer according to claim 1, it is characterized in that: sweating room (2) both sides are provided with chuck, chuck communicates with heating chamber (5), and chuck top one side is provided with vapour outlet (13), discharge of phenolic water mouth (12), and opposite side is provided with water level interface (3).
4, industrial gas phenol liquid vaporizer according to claim 2, it is characterized in that: heating chamber (6) lower body bottom tube sheet (7) top one side is provided with phenol water inlet (10) and clean-up port (9), lower tubesheet (7) below is a cavity, and cavity one side links to each other with gas exit (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620080218 CN2873784Y (en) | 2006-01-13 | 2006-01-13 | Industrial gas phenolic liquid evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620080218 CN2873784Y (en) | 2006-01-13 | 2006-01-13 | Industrial gas phenolic liquid evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2873784Y true CN2873784Y (en) | 2007-02-28 |
Family
ID=37780379
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620080218 Expired - Fee Related CN2873784Y (en) | 2006-01-13 | 2006-01-13 | Industrial gas phenolic liquid evaporator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2873784Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101786697A (en) * | 2010-02-11 | 2010-07-28 | 山东鲁北企业集团总公司 | Processing method and device for purifying acidic sewage by gypsum acid preparation furnace gas |
| CN102583782A (en) * | 2012-03-27 | 2012-07-18 | 宁夏大学 | Method for degrading phenol in waste water in coal chemical industry |
| CN102925220A (en) * | 2012-11-27 | 2013-02-13 | 淄博义丰机械工程有限公司 | Normal pressure phenol water evaporator used for coal gas generator |
| CN103121728A (en) * | 2013-01-28 | 2013-05-29 | 北京德天御投资管理有限责任公司 | Phenol water concentrating device |
-
2006
- 2006-01-13 CN CN 200620080218 patent/CN2873784Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101786697A (en) * | 2010-02-11 | 2010-07-28 | 山东鲁北企业集团总公司 | Processing method and device for purifying acidic sewage by gypsum acid preparation furnace gas |
| CN101786697B (en) * | 2010-02-11 | 2013-07-17 | 山东鲁北企业集团总公司 | Processing method and device for purifying acidic sewage by gypsum acid preparation furnace gas |
| CN102583782A (en) * | 2012-03-27 | 2012-07-18 | 宁夏大学 | Method for degrading phenol in waste water in coal chemical industry |
| CN102583782B (en) * | 2012-03-27 | 2013-03-27 | 宁夏大学 | Method for degrading phenol in waste water in coal chemical industry |
| CN102925220A (en) * | 2012-11-27 | 2013-02-13 | 淄博义丰机械工程有限公司 | Normal pressure phenol water evaporator used for coal gas generator |
| CN103121728A (en) * | 2013-01-28 | 2013-05-29 | 北京德天御投资管理有限责任公司 | Phenol water concentrating device |
| CN103121728B (en) * | 2013-01-28 | 2014-07-09 | 北京德天御投资管理有限责任公司 | Phenol water concentrating device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |