CN108751301A - Environment-friendly type is without fluorescence waste water treatment process of offeing medicine - Google Patents
Environment-friendly type is without fluorescence waste water treatment process of offeing medicine Download PDFInfo
- Publication number
- CN108751301A CN108751301A CN201810729807.7A CN201810729807A CN108751301A CN 108751301 A CN108751301 A CN 108751301A CN 201810729807 A CN201810729807 A CN 201810729807A CN 108751301 A CN108751301 A CN 108751301A
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- Prior art keywords
- waste water
- water
- fluorescence
- fluorescence waste
- vacuum evaporation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/008—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for liquid waste
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- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The present invention relates to technical field of waste water processing, a kind of environment-friendly type is disclosed without fluorescence waste water treatment process of offeing medicine.Include the following steps：(1) fluorescence waste water is subjected to deslagging filtering by the first filtering ponds；(2) filtered fluorescence waste water feeding vacuum evaporation device is evaporated concentration；(3) concentrate feeding combustion chamber is subjected to burning processing.Fluorescence waste water is evaporated concentration by the present invention, utilize the high flammability of concentrate, concentrate is sent into burning Indoor Combustion processing, fluorescence waste water is effectively treated to realize, and heat that burning generates can be efficiently used, process operations of the invention are simple, being capable of meet the requirement of environmental protection, medicament need not be added to be handled, processing cost can be substantially reduced.
Description
Technical field
The present invention relates to technical field of waste water processing, more particularly to a kind of environment-friendly type without fluorescence wastewater treatment work of offeing medicine
Skill.
Background technology
Fluorescence waste water is the waste water that fluorescent penetrant generates after Liquid penetrant testing use, and fluorescent penetrant is Liquid penetrant testing side
Method uses a kind of liquid dye, that is, utilizes the capillarity of liquid, and fluorescent penetrant, which is penetrated into solid material surface opening, to be lacked
Place is fallen into, then the fluorescent penetrant of infiltration is precipitate into the presence of surface display defect by developer.
Contain many kinds of substance such as kerosene, fluorochrome, nonionic surfactant in fluorescence waste water, contains in fluorescence waste water
Harmful components are easy to cause damages to the physical and mental health of ecological environment and people if not in time handled fluorescence waste water.It is existing
There is fluorescence wastewater treatment method that medicament is predominantly added to be handled, agent-feeding treatment method and process flow is complicated, of high cost, medication
Amount is more difficult to control, and treatment effect is unstable, and treated, and water is unable to meet the requirement of environmental protection.
Invention content
The purpose of the invention is to overcome the deficiencies of the prior art and provide a kind of environment-friendly type without fluorescence waste water of offeing medicine at
Science and engineering skill, the process operations are simple, can meet the requirement of environmental protection, and medicament need not be added and handled, can dropped significantly
Reduction process cost.
To achieve the goals above, the present invention provides a kind of environment-friendly type without fluorescence waste water treatment process of offeing medicine, including with
Lower step：
(1) fluorescence waste water is subjected to deslagging filtering by the first filtering ponds；
(2) filtered fluorescence waste water feeding vacuum evaporation device is evaporated concentration, after the filtering
Fluorescence waste water water vapour and concentrate are generated after evaporation and concentration；
(3) concentrate feeding combustion chamber is subjected to burning processing, the heat generated after burning processing is by high-temperature water tank
Interior water heating, the high-temperature water after heating, which enters in the vacuum evaporation device, heats the fluorescence waste water.
Preferably, in the step (1), two layers of filter device, the upper level filter dress are equipped in first filtering ponds
It is set to filter screen, lower layer's filter device is filter paper band.
Preferably, the mesh number of the filter screen is 100 mesh, and the aperture of the filter paper band is 100um.
Preferably, in the step (2), the vacuum evaporation device includes vacuum evaporation room, the vacuum
It is concentrated by evaporation room to connect with vacuum pump, vacuum evaporation ceiling portion is equipped with steam (vapor) outlet, the vacuum evaporation room
Bottom is equipped with concentrated solution outlet, and high-temperature water water inlet, high-temperature water water outlet are respectively equipped on the side wall of the vacuum evaporation room
With fluorescence water intake, the vacuum evaporation chamber interior is equipped with spiral heat exchange tube, and the spiral heat exchange tube upper end passes through
The high-temperature water water inlet is connect with the outlet pipe of the high-temperature water tank, and the spiral heat exchange tube lower end is gone out by the high-temperature water
The mouth of a river is connect with high-temperature water outlet pipe.
Preferably, in the step (2), the condensed device condensation of water vapour becomes distilled water, and the distilled water enters
It is recycled in the high-temperature water tank.
Preferably, in the step (3), the high-temperature water enters after evaporation and concentration processing in the high-temperature water tank
It recycles.
Preferably, in the step (3), the gas that the concentrate generates after the burning Indoor Combustion processing is distinguished
Three-stage filtration is carried out by water curtain, activated carbon and nano-filtration membrane.
Preferably, further include that not used expired fluorescent penetrant is subjected to deslagging filtering, filtering by the second filtering ponds
Fluorescent penetrant afterwards is sent into the combustion chamber and carries out burning processing, and the heat generated after burning processing will be in the high-temperature water tank
Water heating, high-temperature water after heating, which enters in the vacuum evaporation device, heats the fluorescence waste water.
Fluorescence waste water is evaporated concentration by the present invention, and using the high flammability of concentrate, concentrate is sent into combustion chamber
Interior burning processing, is effectively treated fluorescence waste water to realize, and can efficiently use the heat that burning generates, this hair
Bright process operations are simple, can meet the requirement of environmental protection, medicament need not be added and handled, can substantially reduce and be processed into
This.
Description of the drawings
Fig. 1 is the process flow chart of the present invention；
Fig. 2 is the structural schematic diagram of vacuum evaporation device.
Reference sign
1 high-temperature water water inlet, 2 steam (vapor) outlet
3 fluorescence water intake, 4 vacuum evaporation room
5 high-temperature water water outlet, 6 concentrated solution outlet
7 spiral heat exchange tubes
Specific implementation mode
The specific implementation mode of the present invention is described in detail below in conjunction with attached drawing.It should be understood that this place is retouched
The specific implementation mode stated is merely to illustrate and explain the present invention, and is not intended to restrict the invention.
A kind of environment-friendly type of present invention offer is without fluorescence waste water treatment process of offeing medicine, as shown in Figure 1, including the following steps：
(1) fluorescence waste water is subjected to deslagging filtering by the first filtering ponds；
(2) filtered fluorescence waste water feeding vacuum evaporation device is evaporated concentration, after the filtering
Fluorescence waste water water vapour and concentrate are generated after evaporation and concentration；
(3) concentrate feeding combustion chamber is subjected to burning processing, the heat generated after burning processing is by high-temperature water tank
Interior water heating, the high-temperature water after heating, which enters in the vacuum evaporation device, heats the fluorescence waste water.
Fluorescence waste water is evaporated concentration by the present invention, and using the high flammability of concentrate, concentrate is sent into combustion chamber
Interior burning processing, is effectively treated fluorescence waste water to realize, and can efficiently use the heat that burning generates, this hair
Bright process operations are simple, can meet the requirement of environmental protection, medicament need not be added and handled, can substantially reduce and be processed into
This.
In step (1) of the present invention, two layers of filter device, the upper level filter device are equipped in first filtering ponds
For filter screen, lower layer's filter device is filter paper band.Wherein, the mesh number of the filter screen is 100 mesh, the filtering
The aperture of paper tape is 100um.Fluorescence waste water is subjected to two layers of filtration treatment, the solid particle etc. in fluorescence waste water can be effectively removed
Impurity.
In step (2) of the present invention, as shown in Fig. 2, the vacuum evaporation device includes vacuum evaporation room
4, the vacuum evaporation room 4 is connect with vacuum pump, and 4 top of the vacuum evaporation room is equipped with steam (vapor) outlet 2, described true
Sky is concentrated by evaporation 4 bottom of room and is equipped with concentrated solution outlet 6, and high-temperature water water inlet is respectively equipped on 4 side wall of vacuum evaporation room
Mouth 1, high-temperature water water outlet 5 and fluorescence water intake 3, the vacuum evaporation room 4 are internally provided with spiral heat exchange tube 7, institute
It states 7 upper end of spiral heat exchange tube to connect with the outlet pipe of the high-temperature water tank by the high-temperature water water inlet 1, the spiral heat exchange
7 lower end of pipe is connect by the high-temperature water water outlet 5 with high-temperature water outlet pipe.
The course of work of the wherein described vacuum evaporation device is：High-temperature water in the high-temperature water tank is through the high temperature
Water water inlet 1 enters in the spiral heat exchange tube 7, high-temperature water circulation in the spiral heat exchange tube 7, thus with entrance
Fluorescence waste water carries out heat exchange, and fluorescence waste water is heated, and low-temperature evaporation, generation water vapour are glimmering under vacuum conditions for fluorescence waste water
Become fluorescence Waste water concentrating liquid after moisture evaporation in light waste water, is condensed wherein the water vapour enters through the steam (vapor) outlet 2
Device becomes distilled water through condenser condensation, and the distilled water, which can enter in the high-temperature water tank, to be recycled, that is, is continued
High-temperature water is heated as into use in the vacuum evaporation room 4, to recycle water resource, avoids water resource unrestrained
Take, reaches energy-saving and environment-friendly effect.
Preferably, in the step (3), the high-temperature water enters after evaporation and concentration processing in the high-temperature water tank
It recycles, i.e., enters the height through the high-temperature water outlet pipe after the fluorescence waste water progress heat exchange of the described high-temperature water and entrance
In reservoir, continue to be heated as high-temperature water into using in the vacuum evaporation room 4, to recycle water resource,
Water resource waste is avoided, energy-saving and environment-friendly effect is reached.
Preferably, in the step (3), the gas that the concentrate generates after the burning Indoor Combustion processing is distinguished
Three-stage filtration is carried out by water curtain, activated carbon and nano-filtration membrane.What the concentrate generated after the burning Indoor Combustion
Water vapour and carbide dust are mainly contained in gas, and the dust in gas can be effectively sponged by three-stage filtration, it is real
The environment protection emission of existing burning gases, to be further ensured that fluorescence wastewater treatment meet the requirement of environmental protection.
In addition to fluorescence waste water is handled, not used expired fluorescent penetrant is also required to be handled, the present invention
Not used expired fluorescent penetrant is subjected to deslagging filtering by the second filtering ponds, with the deslagging filtering one of above-mentioned fluorescence waste water
Sample also is provided with two layers of filter device in second filtering ponds, and the upper level filter device is filter screen, lower layer's filtering
Device is filter paper band, and not used expired fluorescent penetrant is carried out two layers of filtration treatment, can effectively remove not used mistake
The impurity such as the solid particle in phase fluorescent penetrant.Since not used expired fluorescent penetrant itself has high flammability, because
This need not be evaporated concentration, can filtered fluorescent penetrant be directly sent into the combustion chamber and carried out at burning
Reason, the heat generated after burning processing heat the water in the high-temperature water tank, and the high-temperature water after heating is steamed into the vacuum
For being heated to above-mentioned fluorescence waste water in hair enrichment facility.
The preferred embodiment of the present invention is described in detail above in association with attached drawing, still, the present invention is not limited to above-mentioned realities
The detail in mode is applied, within the scope of the technical concept of the present invention, a variety of letters can be carried out to technical scheme of the present invention
Monotropic type, these simple variants all belong to the scope of protection of the present invention.
It is further to note that specific technical features described in the above specific embodiments, in not lance
In the case of shield, can be combined by any suitable means, in order to avoid unnecessary repetition, the present invention to it is various can
The combination of energy no longer separately illustrates.
In addition, various embodiments of the present invention can be combined randomly, as long as it is without prejudice to originally
The thought of invention, it should also be regarded as the disclosure of the present invention.
Claims (8)
1. a kind of environment-friendly type is without fluorescence waste water treatment process of offeing medicine, which is characterized in that include the following steps：
(1) fluorescence waste water is subjected to deslagging filtering by the first filtering ponds；
(2) filtered fluorescence waste water feeding vacuum evaporation device is evaporated concentration, it is described filtered glimmering
Light waste water generates water vapour and concentrate after evaporation and concentration；
(3) concentrate feeding combustion chamber is subjected to burning processing, the heat generated after burning processing will be in high-temperature water tank
Water heats, and the high-temperature water after heating, which enters in the vacuum evaporation device, heats the fluorescence waste water.
2. environment-friendly type according to claim 1 is without fluorescence waste water treatment process of offeing medicine, which is characterized in that the step
(1) in, two layers of filter device is equipped in first filtering ponds, the upper level filter device is filter screen, lower layer's mistake
Filter device is filter paper band.
3. environment-friendly type according to claim 2 is without fluorescence waste water treatment process of offeing medicine, which is characterized in that the filter wire
The mesh number of net is 100 mesh, and the aperture of the filter paper band is 100um.
4. environment-friendly type according to claim 1 is without fluorescence waste water treatment process of offeing medicine, which is characterized in that the step
(2) in, the vacuum evaporation device includes vacuum evaporation room (4), the vacuum evaporation room (4) and vacuum pump
Connection, vacuum evaporation room (4) top are equipped with steam (vapor) outlet (2), and vacuum evaporation room (4) bottom is equipped with dense
Contracting liquid exports (6), and high-temperature water water inlet (1), high-temperature water water outlet are respectively equipped on vacuum evaporation room (4) side wall
(5) and fluorescence water intake (3), the vacuum evaporation room (4) are internally provided with spiral heat exchange tube (7), and the spiral is changed
Heat pipe (7) upper end is connect by the high-temperature water water inlet (1) with the outlet pipe of the high-temperature water tank, the spiral heat exchange tube
(7) lower end is connect by the high-temperature water water outlet (5) with high-temperature water outlet pipe.
5. environment-friendly type according to claim 1 is without fluorescence waste water treatment process of offeing medicine, which is characterized in that the step
(2) in, the condensed device condensation of water vapour becomes distilled water, and the distilled water, which enters in the high-temperature water tank, to be recycled.
6. environment-friendly type according to claim 1 is without fluorescence waste water treatment process of offeing medicine, which is characterized in that the step
(3) in, the high-temperature water, which enters after evaporation and concentration processing in the high-temperature water tank, to be recycled.
7. environment-friendly type according to claim 1 is without fluorescence waste water treatment process of offeing medicine, which is characterized in that the step
(3) in, the gas that the concentrate generates after the burning Indoor Combustion processing is respectively by water curtain, activated carbon and nanometer mistake
Filter membrane carries out three-stage filtration.
8. environment-friendly type according to claim 1 is without fluorescence waste water treatment process of offeing medicine, which is characterized in that further including will not
The expired fluorescent penetrant used carries out deslagging filtering by the second filtering ponds, and filtered fluorescent penetrant is sent into the burning
Room carries out burning processing, and the heat generated after burning processing heats the water in the high-temperature water tank, the high-temperature water after heating into
Enter and the fluorescence waste water is heated in the vacuum evaporation device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810729807.7A CN108751301A (en) | 2018-07-05 | 2018-07-05 | Environment-friendly type is without fluorescence waste water treatment process of offeing medicine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810729807.7A CN108751301A (en) | 2018-07-05 | 2018-07-05 | Environment-friendly type is without fluorescence waste water treatment process of offeing medicine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108751301A true CN108751301A (en) | 2018-11-06 |
Family
ID=63972476
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810729807.7A Pending CN108751301A (en) | 2018-07-05 | 2018-07-05 | Environment-friendly type is without fluorescence waste water treatment process of offeing medicine |
Country Status (1)
| Country | Link |
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| CN (1) | CN108751301A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113526592A (en) * | 2021-07-29 | 2021-10-22 | 董春 | Large-scale high-salinity wastewater desalting device and large-scale high-salinity wastewater desalting method thereof |
Citations (5)
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|---|---|---|---|---|
| DE2360491B1 (en) * | 1973-12-05 | 1974-10-03 | Franz Dipl.-Ing. 7400 Tuebingen Koeppl | Industrial effluent purificn. - e.g. wash water from a dye works with recovery of salt-free sterile water |
| CN1485280A (en) * | 2003-08-22 | 2004-03-31 | 清华大学 | Two-stage immersion combustion evaporation process for treating percolate from filling field |
| CN202048575U (en) * | 2011-01-11 | 2011-11-23 | 烟台绿环再生资源有限公司 | High concentration organic waste water concentration and incineration disposal line |
| CN103482715A (en) * | 2013-09-16 | 2014-01-01 | 惠州Tcl环境科技有限公司 | High-concentration organic waste water evaporating and concentration processing method |
| CN207342234U (en) * | 2017-08-29 | 2018-05-11 | 天津普罗米新材料有限公司 | One kind vacuum distillation recycling machine |
-
2018
- 2018-07-05 CN CN201810729807.7A patent/CN108751301A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2360491B1 (en) * | 1973-12-05 | 1974-10-03 | Franz Dipl.-Ing. 7400 Tuebingen Koeppl | Industrial effluent purificn. - e.g. wash water from a dye works with recovery of salt-free sterile water |
| CN1485280A (en) * | 2003-08-22 | 2004-03-31 | 清华大学 | Two-stage immersion combustion evaporation process for treating percolate from filling field |
| CN202048575U (en) * | 2011-01-11 | 2011-11-23 | 烟台绿环再生资源有限公司 | High concentration organic waste water concentration and incineration disposal line |
| CN103482715A (en) * | 2013-09-16 | 2014-01-01 | 惠州Tcl环境科技有限公司 | High-concentration organic waste water evaporating and concentration processing method |
| CN207342234U (en) * | 2017-08-29 | 2018-05-11 | 天津普罗米新材料有限公司 | One kind vacuum distillation recycling machine |
Non-Patent Citations (2)
| Title |
|---|
| 翁长淦: "《化工无损探伤工工艺学》", 31 March 1988, 成都科技大学出版社 * |
| 黄业茹等: "《持久性有机污染物调查监控与预警技术》", 30 April 2009, 中国环境科学出版社 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113526592A (en) * | 2021-07-29 | 2021-10-22 | 董春 | Large-scale high-salinity wastewater desalting device and large-scale high-salinity wastewater desalting method thereof |
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| PB01 | Publication | ||
| PB01 | Publication | ||
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| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181106 |
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| RJ01 | Rejection of invention patent application after publication |