CN106186483A - High chlorine high salt liquid waste treatment system - Google Patents
High chlorine high salt liquid waste treatment system Download PDFInfo
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- CN106186483A CN106186483A CN201510224085.6A CN201510224085A CN106186483A CN 106186483 A CN106186483 A CN 106186483A CN 201510224085 A CN201510224085 A CN 201510224085A CN 106186483 A CN106186483 A CN 106186483A
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- liquid
- outfan
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- room
- heater
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Abstract
The invention discloses a kind of high chlorine high salt liquid waste treatment system, including waste liquid storage tank, it is additionally provided with the pretreatment tank that the outfan with waste liquid storage tank is connected, the heater being connected with the outfan of pretreatment tank, heater is additionally provided with primary steam input pipe, the gas-liquid separator being connected with the outfan of heater, the top of gas-liquid separator is connected by indirect steam outlet tube Mechanical Vapor Compression, the solid-liquid outfan of gas-liquid separator completes solid material output through solid-liquid filter, the remaining liq of solid-liquid filter is connected with pretreatment tank through secondary recovery mother liquor tank simultaneously, the fluid output port synchronizing gas-liquid separator is connected with pretreatment tank by circulating pump, it is also associated with vacuum pumping pump on the heaters.The simple in construction of the present invention, saves energy utilization rate, can effectively complete the process to high chlorine height bisulfate waste liquor, can effectively reduce the cost of liquid waste processing simultaneously, improves treatment effeciency, and the suitability is strong, and practicality is good.
Description
Technical field
The invention belongs to high chlorine high salt liquid waste disposal technique field, be specifically related to a kind of high chlorine height bisulfate waste liquor
Processing system.
Background technology
Along with the fast development of China's economy, various medicine, food, chemical industry and oil etc. produce and refine
Technique have also been obtained effective development, but it is high typically to produce a large amount of high chlorine in producing extractive process
The waste liquids such as salt, prior art uses biochemical processing process to process mostly, and due to high chlorine high salt
Waste liquid biochemical treatment difficulty is bigger, it is difficult to directly process, and uses concentration technology to be processed into simultaneously
This is higher, and automaticity is relatively low simultaneously, it is difficult to meet the demand of market development.
Summary of the invention
It is an object of the invention to provide a kind of simple in construction, can effectively process high chlorine height bisulfate waste liquor and process
The high chlorine high salt liquid waste treatment system that low cost, efficiency are high.
The technical scheme realizing the object of the invention is a kind of high chlorine high salt liquid waste treatment system, including waste liquid
Storage tank, is additionally provided with the pretreatment tank that the outfan with described waste liquid storage tank is connected, pre-with described
The heater that the outfan of process tank is connected, is additionally provided with primary steam input on described heater
Pipe, the gas-liquid separator being connected with the outfan of described heater, the top of described gas-liquid separator
Connected by indirect steam outlet tube and have Mechanical Vapor Compression, the output of described Mechanical Vapor Compression
End is connected with described heater by indirect steam input, the solid-liquid output of described gas-liquid separator
Hold and complete solid material output, the remaining liq warp of the most described solid-liquid filter through solid-liquid filter
Crossing secondary recovery mother liquor tank to be connected with described pretreatment tank, the liquid synchronizing described gas-liquid separator is defeated
Go out end to be connected with described pretreatment tank by circulating pump, described heater is also associated with evacuation
Pump.
Described gas-liquid separator includes housing, and the upper end in described housing is provided with negative pressure vaporizer,
Middle-end in described housing is provided with crystallized liquid room, is provided with charging aperture, liquid defeated on described housing
Going out end and solid-liquid outfan, described charging aperture is connected with described negative pressure vaporizer, and described liquid exports
End be arranged on described crystallization liquefied room and described negative pressure vaporizer connection and described fluid output port with
Described crystallization liquefied room is connected, and described solid-liquid outfan is arranged on the bottom of housing, at described housing
Top be provided with steam (vapor) outlet, described steam (vapor) outlet is connected with described negative pressure vaporizer, described solid-liquid
Stiff room, described stiff room and described solid-liquid outfan it is provided with between outfan and described crystallized liquid room
Being connected, be additionally provided with anti-cyclone funnel in described housing, described anti-cyclone funnel is arranged on described negative
Between pressure vaporizer and described crystallized liquid room, it is provided with vertical water conservancy diversion at the center of described crystallized liquid room
Cylinder, the top of described vertical guide shell is connected, in institute with the bottom osculum end of described anti-cyclone funnel
The bottom stating vertical guide shell is provided with level rotary flow plate, and described level rotary flow plate is arranged on described stiff room
Top, the inwall of described crystallized liquid room is transversely provided with the brilliant plate of gear, described gear crystalline substance plate is arranged on
Described go out fluid output port lower section.
Described heater is MVR negative pressure antiscale heater.
The present invention has a positive effect: the simple in construction of the present invention, sets at the top of gas-liquid separator
There is indirect steam outlet tube, and indirect steam outlet tube is steamed by secondary through Mechanical Vapor Compression again
Vapour input pipe is connected with heater, makes low-pressure low-temperature steam obtain effectively again with, certain journey
Save energy utilization rate on degree, and use the structure of present patent application, can effectively complete height
The process of chlorine height bisulfate waste liquor, and its automaticity is relatively strong, can effectively reduce liquid waste processing simultaneously
Cost, improves treatment effeciency, and the suitability is strong, and practicality is good.
Accompanying drawing explanation
In order to make present disclosure be more likely to be clearly understood, below according to specific embodiment and tie
Closing accompanying drawing, the present invention is further detailed explanation, wherein:
Fig. 1 is the population structure schematic diagram of the present invention；
Fig. 2 is the concrete structure schematic diagram of gas-liquid separator in Fig. 1.
Detailed description of the invention
(embodiment 1)
Fig. 1 and Fig. 2 shows a kind of detailed description of the invention of the present invention, and wherein Fig. 1 is the present invention's
Population structure schematic diagram；Fig. 2 is the concrete structure schematic diagram of gas-liquid separator in Fig. 1.
See Fig. 1 and Fig. 2, a kind of high chlorine high salt liquid waste treatment system, including waste liquid storage tank 1, also set
There is the pretreatment tank 2 that the outfan with described waste liquid storage tank 1 is connected, with described pretreatment tank 2
The heater 3 that outfan is connected, is additionally provided with primary steam input pipe 4 on described heater 3,
The gas-liquid separator 5 being connected with the outfan of described heater 3, the top of described gas-liquid separator 5
Connected by indirect steam outlet tube 6 and have Mechanical Vapor Compression 7, described Mechanical Vapor Compression 7
Outfan is connected with described heater 3 by indirect steam input 8, described gas-liquid separator 5
Solid-liquid outfan 51 through solid-liquid filter 9 complete solid material output, the most described solid-liquid filtration
The remaining liq of device 9 is connected with described pretreatment tank 2 through secondary recovery mother liquor tank 10, synchronizes institute
The fluid output port 52 stating gas-liquid separator 5 is connected with described pretreatment tank 2 by circulating pump 11,
Described heater 3 is also associated with vacuum pumping pump 12.
Described gas-liquid separator 5 includes housing 53, and the upper end in described housing 53 is provided with negative pressure vaporization
Room 54, the middle-end in described housing 53 is provided with crystallized liquid room 55, sets on described housing 53
There are charging aperture 56, fluid output port 52 and solid-liquid outfan 51, described charging aperture 56 and described negative pressure
Vaporizer 54 is connected, and it is negative with described that described fluid output port 52 is arranged on described crystallization liquefied room 55
Pressure vaporizer 54 connection and described fluid output port 52 are connected with described crystallization liquefied room 55,
Described solid-liquid outfan 51 is arranged on the bottom of housing 53, is provided with steam at the top of described housing 53
Outlet 57, described steam (vapor) outlet 57 is connected with described negative pressure vaporizer 54, described solid-liquid outfan
Being provided with stiff room 58 between 51 and described crystallized liquid room 55, described stiff room 58 is defeated with described solid-liquid
Go out end 51 to be connected, in described housing 53, be additionally provided with anti-cyclone funnel 59, described anti-cyclone funnel
59 are arranged between described negative pressure vaporizer 54 and described crystallized liquid room 55, at described crystallized liquid
The center of room 55 is provided with vertical guide shell 510, the top of described vertical guide shell 510 and described anti-rotation
The bottom osculum end of stream funnel 59 is connected, and is provided with level rotation in the bottom of described vertical guide shell 510
Stream plate 511, described level rotary flow plate 511 is arranged on the top of described stiff room 58, in described crystallization
Be transversely provided with the brilliant plate 512 of gear on the inwall of liquid chamber 55, the brilliant plate 512 of described gear be arranged on described in go out liquid
The lower section of body outfan 52.
Described heater 3 is MVR negative pressure antiscale heater.
Obviously, the above embodiment of the present invention is only for clearly demonstrating example of the present invention,
And it is not the restriction to embodiments of the present invention.For those of ordinary skill in the field,
Can also make other changes in different forms on the basis of the above description.Here without also
Cannot all of embodiment be given exhaustive.And these connotations belonging to the present invention are extended out
Obvious change or variation still fall within protection scope of the present invention.
Claims (3)
1. a high chlorine high salt liquid waste treatment system, including waste liquid storage tank, it is characterised in that: also set
There is the pretreatment tank that the outfan with described waste liquid storage tank is connected, with the output of described pretreatment tank
The heater that end is connected, is additionally provided with primary steam input pipe on described heater, adds with described
The gas-liquid separator that the outfan of hot device is connected, indirect steam is passed through at the top of described gas-liquid separator
Outlet tube connects has Mechanical Vapor Compression, the outfan of described Mechanical Vapor Compression to be steamed by secondary
Vapour input is connected with described heater, and the solid-liquid outfan of described gas-liquid separator is through solid-liquid mistake
Filter completes solid material output, and the remaining liq of the most described solid-liquid filter is female through secondary recovery
Flow container is connected with described pretreatment tank, synchronizes the fluid output port of described gas-liquid separator by circulation
Pump is connected with described pretreatment tank, is also associated with vacuum pumping pump on described heater.
High chlorine high salt liquid waste treatment system the most according to claim 1, it is characterised in that: described
Gas-liquid separator includes housing, and the upper end in described housing is provided with negative pressure vaporizer, at described housing
Interior middle-end is provided with crystallized liquid room, is provided with charging aperture, fluid output port and consolidates on described housing
Liquid outfan, described charging aperture is connected with described negative pressure vaporizer, and described fluid output port is arranged on
Described crystallization liquefied room and described negative pressure vaporizer connection and described fluid output port and described crystallization
Liquefied room is connected, and described solid-liquid outfan is arranged on the bottom of housing, sets at the top of described housing
Have steam (vapor) outlet, described steam (vapor) outlet to be connected with described negative pressure vaporizer, described solid-liquid outfan with
Being provided with stiff room between described crystallized liquid room, described stiff room is connected with described solid-liquid outfan,
Being additionally provided with anti-cyclone funnel in described housing, described anti-cyclone funnel is arranged on described negative pressure vaporizer
And between described crystallized liquid room, it is provided with vertical guide shell at the center of described crystallized liquid room, described
The vertical top of guide shell is connected with the bottom osculum end of described anti-cyclone funnel, vertically leads described
The bottom of flow cartridge is provided with level rotary flow plate, and described level rotary flow plate is arranged on the top of described stiff room,
The inwall of described crystallized liquid room is transversely provided with the brilliant plate of gear, described gear crystalline substance plate be arranged on described in go out liquid
The lower section of body outfan.
High chlorine high salt liquid waste treatment system the most according to claim 2, it is characterised in that: described
Heater is MVR negative pressure antiscale heater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510224085.6A CN106186483A (en) | 2015-05-06 | 2015-05-06 | High chlorine high salt liquid waste treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510224085.6A CN106186483A (en) | 2015-05-06 | 2015-05-06 | High chlorine high salt liquid waste treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106186483A true CN106186483A (en) | 2016-12-07 |
Family
ID=57458826
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510224085.6A Pending CN106186483A (en) | 2015-05-06 | 2015-05-06 | High chlorine high salt liquid waste treatment system |
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| Country | Link |
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| CN (1) | CN106186483A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109865302A (en) * | 2019-03-15 | 2019-06-11 | 南京航空航天大学 | Intermittent MVR storage heat is for thermal evaporation system and its working method |
| CN113575358A (en) * | 2021-08-19 | 2021-11-02 | 深圳市南方卉谷科技有限公司 | Ingredient of planting matrix and preparation method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203095629U (en) * | 2013-03-16 | 2013-07-31 | 上虞市佳和化工有限公司 | Sodium chloride recycling and crystallizing device |
| US20140186242A1 (en) * | 2010-09-28 | 2014-07-03 | Trailblazer Technologies (Pty) Ltd | Water treatment |
| CN203852860U (en) * | 2014-05-09 | 2014-10-01 | 重庆山巨化工机械有限公司 | Vapor-liquid separating crystallization device |
| CN204803163U (en) * | 2015-05-06 | 2015-11-25 | 重庆山巨化工机械有限公司 | High salt liquid water disposal system of high chlorine |
-
2015
- 2015-05-06 CN CN201510224085.6A patent/CN106186483A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140186242A1 (en) * | 2010-09-28 | 2014-07-03 | Trailblazer Technologies (Pty) Ltd | Water treatment |
| CN203095629U (en) * | 2013-03-16 | 2013-07-31 | 上虞市佳和化工有限公司 | Sodium chloride recycling and crystallizing device |
| CN203852860U (en) * | 2014-05-09 | 2014-10-01 | 重庆山巨化工机械有限公司 | Vapor-liquid separating crystallization device |
| CN204803163U (en) * | 2015-05-06 | 2015-11-25 | 重庆山巨化工机械有限公司 | High salt liquid water disposal system of high chlorine |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109865302A (en) * | 2019-03-15 | 2019-06-11 | 南京航空航天大学 | Intermittent MVR storage heat is for thermal evaporation system and its working method |
| CN113575358A (en) * | 2021-08-19 | 2021-11-02 | 深圳市南方卉谷科技有限公司 | Ingredient of planting matrix and preparation method thereof |
| CN113575358B (en) * | 2021-08-19 | 2023-10-20 | 深圳市南方卉谷科技有限公司 | Ingredients of planting matrix and preparation method thereof |
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Application publication date: 20161207 |