CN204803163U - High salt liquid water disposal system of high chlorine - Google Patents
High salt liquid water disposal system of high chlorine Download PDFInfo
- Publication number
- CN204803163U CN204803163U CN201520284949.9U CN201520284949U CN204803163U CN 204803163 U CN204803163 U CN 204803163U CN 201520284949 U CN201520284949 U CN 201520284949U CN 204803163 U CN204803163 U CN 204803163U
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- Prior art keywords
- liquid
- solid
- room
- output terminal
- well heater
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Abstract
The utility model discloses a high salt liquid water disposal system of high chlorine, including waste liquid storage jar, still be equipped with the pretreatment tank who is connected with the output of waste liquid storage jar, the heater that is connected with pretreatment tank's output, still be equipped with the primary steam input tube on the heater, the vapour and liquid separator who is connected with the output of heater, there is mechanical vapor compressor at vapour and liquid separator's top through flash steam output tube connected, solid material output is accomplished through the solid -liquid filter to vapour and liquid separator's solid -liquid output, the surplus liquid of solid -liquid filter is linked together with pretreatment tank through secondary recovery mother liquor tank simultaneously, synchronous vapour and liquid separator's liquid output is linked together with pretreatment tank through the circulating pump, still be connected with the evacuation pump on the heater. The utility model has the advantages of simple structure, has saved energy utilization and has rateed, can effectual completion to the processing of the high salt waste liquid of high chlorine, cost that simultaneously can effectual reduction liquid water disposal improves the treatment effeciency, the suitability is strong, the practicality is good.
Description
Technical field
The utility model belongs to high chlorine height bisulfate waste liquor processing technology field, is specifically related to a kind of high chlorine height bisulfate waste liquor treatment system.
Background technology
Along with the fast development of China's economy, various medicine, food, chemical industry and oil etc. are produced refining technique and be have also been obtained effective development, but the waste liquids such as a large amount of high chlorine height salt generally can be produced in production extractive process, prior art adopts biochemical processing process to process mostly, and due to high chlorine height bisulfate waste liquor biochemical treatment difficulty comparatively large, be difficult to direct process, adopt concentration technology to carry out processing cost higher simultaneously, level of automation is also lower simultaneously, is difficult to the demand meeting market development.
Utility model content
It is simple that the purpose of this utility model is to provide a kind of structure, effectively can process high chlorine height bisulfate waste liquor and the high chlorine height bisulfate waste liquor treatment system that processing cost is low, efficiency is high.
The technical scheme realizing the utility model object is a kind of high chlorine height bisulfate waste liquor treatment system, comprise waste liquid storage tank, also be provided with the pre-treatment tank be connected with the output terminal of described waste liquid storage tank, the well heater be connected with the output terminal of described pre-treatment tank, primary steam input tube is also provided with in the upper of described well heater, the gas-liquid separator be connected with the output terminal of described well heater, the top of described gas-liquid separator is connected with Mechanical Vapor Compression by secondary steam output tube, the output terminal of described Mechanical Vapor Compression is connected with described well heater by secondary steam input terminus, the solid-liquid output terminal of described gas-liquid separator completes solid materials through solid-liquid filter and exports, the remaining liq of described solid-liquid filter is connected with described pre-treatment tank through secondary recovery mother liquor tank simultaneously, the fluid output port of synchronous described gas-liquid separator is connected with described pre-treatment tank by recycle pump, described well heater is also connected with vacuum pumping pump.
Described gas-liquid separator comprises housing, upper end in described housing is provided with negative pressure vaporizing chamber, middle-end in described housing is provided with crystallized liquid room, described housing is provided with opening for feed, fluid output port and solid-liquid output terminal, described opening for feed is connected with described negative pressure vaporizing chamber, described fluid output port be arranged on described crystallization liquefied room with described negative pressure vaporizing chamber connection and described fluid output port be connected with described crystallization liquefied room, described solid-liquid output terminal is arranged on the bottom of housing, vapour outlet is provided with at the top of described housing, described vapour outlet is connected with described negative pressure vaporizing chamber, stiff room is provided with between described solid-liquid output terminal and described crystallized liquid room, described stiff room is connected with described solid-liquid output terminal, anti-cyclone funnel is also provided with in described housing, described anti-cyclone funnel is arranged between described negative pressure vaporizing chamber and described crystallized liquid room, vertical guide shell is provided with at the center of described crystallized liquid room, the top of described vertical guide shell is connected with the bottom osculum end of described anti-cyclone funnel, level rotary flow plate is provided with in the bottom of described vertical guide shell, described level rotary flow plate is arranged on the top of described stiff room, the inwall of described crystallized liquid room is laterally provided with the brilliant plate of gear, the below of fluid output port is gone out described in the brilliant plate of described gear is arranged on.
Described well heater is MVR negative pressure antiscale well heater.
The utility model has positive effect: structure of the present utility model is simple, secondary steam output tube is provided with at the top of gas-liquid separator, and secondary steam output tube is connected with well heater by secondary steam input tube through Mechanical Vapor Compression again, low-pressure low-temperature steam is made to obtain effectively again utilizing, save energy utilization rate to a certain extent, and adopt the structure of present patent application, effectively can complete the process to high chlorine height bisulfate waste liquor, and its level of automation is stronger, the cost of liquid waste disposal can be effectively reduced simultaneously, improve processing efficiency, suitability is strong, practicality is good.
Accompanying drawing explanation
In order to make content of the present utility model be more likely to be clearly understood, below according to specific embodiment also by reference to the accompanying drawings, the utility model is described in further detail, wherein:
Fig. 1 is overall structure schematic diagram of the present utility model;
Fig. 2 is the concrete structure schematic diagram of gas-liquid separator in Fig. 1.
Embodiment
(embodiment 1)
Fig. 1 and Fig. 2 shows a kind of embodiment of the present utility model, and wherein Fig. 1 is overall structure schematic diagram of the present utility model; 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 height bisulfate waste liquor treatment system, comprise waste liquid storage tank 1, also be provided with the pre-treatment tank 2 be connected with the output terminal of described waste liquid storage tank 1, the well heater 3 be connected with the output terminal of described pre-treatment tank 2, primary steam input tube 4 is also provided with in the upper of described well heater 3, the gas-liquid separator 5 be connected with the output terminal of described well heater 3, the top of described gas-liquid separator 5 is connected with Mechanical Vapor Compression 7 by secondary steam output tube 6, the output terminal of described Mechanical Vapor Compression 7 is connected with described well heater 3 by secondary steam input terminus 8, the solid-liquid output terminal 51 of described gas-liquid separator 5 completes solid materials through solid-liquid filter 9 and exports, the remaining liq of described solid-liquid filter 9 is connected with described pre-treatment tank 2 through secondary recovery mother liquor tank 10 simultaneously, the fluid output port 52 of synchronous described gas-liquid separator 5 is connected with described pre-treatment tank 2 by recycle pump 11, described well heater 3 is also connected with vacuum pumping pump 12.
Described gas-liquid separator 5 comprises housing 53, upper end in described housing 53 is provided with negative pressure vaporizing chamber 54, middle-end in described housing 53 is provided with crystallized liquid room 55, described housing 53 is provided with opening for feed 56, fluid output port 52 and solid-liquid output terminal 51, described opening for feed 56 is connected with described negative pressure vaporizing chamber 54, described fluid output port 52 be arranged on described crystallization liquefied room 55 with described negative pressure vaporizing chamber 54 connection and described fluid output port 52 be connected with described crystallization liquefied room 55, described solid-liquid output terminal 51 is arranged on the bottom of housing 53, vapour outlet 57 is provided with at the top of described housing 53, described vapour outlet 57 is connected with described negative pressure vaporizing chamber 54, stiff room 58 is provided with between described solid-liquid output terminal 51 and described crystallized liquid room 55, described stiff room 58 is connected with described solid-liquid output terminal 51, anti-cyclone funnel 59 is also provided with in described housing 53, described anti-cyclone funnel 59 is arranged between described negative pressure vaporizing chamber 54 and described crystallized liquid room 55, vertical guide shell 510 is provided with at the center of described crystallized liquid room 55, the top of described vertical guide shell 510 is connected with the bottom osculum end of described anti-cyclone funnel 59, level rotary flow plate 511 is provided with in the bottom of described vertical guide shell 510, described level rotary flow plate 511 is arranged on the top of described stiff room 58, the inwall of described crystallized liquid room 55 is laterally provided with the brilliant plate 512 of gear, the below of fluid output port 52 is gone out described in the brilliant plate 512 of described gear is arranged on.
Described well heater 3 is MVR negative pressure antiscale well heater.
Obviously, above-described embodiment of the present utility model is only for the utility model example is clearly described, and is not the restriction to embodiment of the present utility model.For those of ordinary skill in the field, can also make other changes in different forms on the basis of the above description.Here exhaustive without the need to also giving all embodiments.And these belong to connotation of the present utility model the apparent change of extending out or variation still belong to protection domain of the present utility model.
Claims (3)
1. one kind high chlorine height bisulfate waste liquor treatment system, comprise waste liquid storage tank, it is characterized in that: be also provided with the pre-treatment tank be connected with the output terminal of described waste liquid storage tank, the well heater be connected with the output terminal of described pre-treatment tank, primary steam input tube is also provided with in the upper of described well heater, the gas-liquid separator be connected with the output terminal of described well heater, the top of described gas-liquid separator is connected with Mechanical Vapor Compression by secondary steam output tube, the output terminal of described Mechanical Vapor Compression is connected with described well heater by secondary steam input terminus, the solid-liquid output terminal of described gas-liquid separator completes solid materials through solid-liquid filter and exports, the remaining liq of described solid-liquid filter is connected with described pre-treatment tank through secondary recovery mother liquor tank simultaneously, the fluid output port of synchronous described gas-liquid separator is connected with described pre-treatment tank by recycle pump, described well heater is also connected with vacuum pumping pump.
2. high chlorine height bisulfate waste liquor treatment system according to claim 1, it is characterized in that: described gas-liquid separator comprises housing, upper end in described housing is provided with negative pressure vaporizing chamber, middle-end in described housing is provided with crystallized liquid room, described housing is provided with opening for feed, fluid output port and solid-liquid output terminal, described opening for feed is connected with described negative pressure vaporizing chamber, described fluid output port be arranged on described crystallization liquefied room with described negative pressure vaporizing chamber connection and described fluid output port be connected with described crystallization liquefied room, described solid-liquid output terminal is arranged on the bottom of housing, vapour outlet is provided with at the top of described housing, described vapour outlet is connected with described negative pressure vaporizing chamber, stiff room is provided with between described solid-liquid output terminal and described crystallized liquid room, described stiff room is connected with described solid-liquid output terminal, anti-cyclone funnel is also provided with in described housing, described anti-cyclone funnel is arranged between described negative pressure vaporizing chamber and described crystallized liquid room, vertical guide shell is provided with at the center of described crystallized liquid room, the top of described vertical guide shell is connected with the bottom osculum end of described anti-cyclone funnel, level rotary flow plate is provided with in the bottom of described vertical guide shell, described level rotary flow plate is arranged on the top of described stiff room, the inwall of described crystallized liquid room is laterally provided with the brilliant plate of gear, the brilliant plate of described gear is arranged on the below of described fluid output port.
3. high chlorine height bisulfate waste liquor treatment system according to claim 2, is characterized in that: described well heater is MVR negative pressure antiscale well heater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520284949.9U CN204803163U (en) | 2015-05-06 | 2015-05-06 | High salt liquid water disposal system of high chlorine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520284949.9U CN204803163U (en) | 2015-05-06 | 2015-05-06 | High salt liquid water disposal system of high chlorine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204803163U true CN204803163U (en) | 2015-11-25 |
Family
ID=54588017
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520284949.9U Expired - Fee Related CN204803163U (en) | 2015-05-06 | 2015-05-06 | High salt liquid water disposal system of high chlorine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204803163U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106186483A (en) * | 2015-05-06 | 2016-12-07 | 重庆山巨化工机械有限公司 | High chlorine high salt liquid waste treatment system |
-
2015
- 2015-05-06 CN CN201520284949.9U patent/CN204803163U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106186483A (en) * | 2015-05-06 | 2016-12-07 | 重庆山巨化工机械有限公司 | High chlorine high salt liquid waste treatment system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 401147 Longhua Avenue, Yubei District, Chongqing 1889 California lilies garden A 21-1 Patentee after: Chongqing mountain giant chemical machinery Limited by Share Ltd Address before: 400900 Longhua Avenue, Yubei District, Chongqing 1889 California lilies garden A 21-1 Patentee before: Chongqing Shan Ju chemical machinery Co., Ltd |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151125 Termination date: 20200506 |