CN107140780A - A kind of spent acid single effect evaporation processing unit - Google Patents
A kind of spent acid single effect evaporation processing unit Download PDFInfo
- Publication number
- CN107140780A CN107140780A CN201710567359.0A CN201710567359A CN107140780A CN 107140780 A CN107140780 A CN 107140780A CN 201710567359 A CN201710567359 A CN 201710567359A CN 107140780 A CN107140780 A CN 107140780A
- Authority
- CN
- China
- Prior art keywords
- tank
- separator
- crystallisation
- cooling kettle
- spent acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
-
- 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
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F2001/5218—Crystallization
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a kind of spent acid single effect evaporation processing unit, mainly by spent acid groove, filter, evaporator, separator, crystallisation by cooling kettle, centrifuge, reclaim acid tank, condenser, reclaim tank, vacuum buffer tank and vacuum pump assembly composition, described filter is arranged on the right of spent acid groove, filter upper right side is provided with separator, the separator upper left corner is connected with filter, the separator left side is connected with each other provided with evaporator and with separator, crystallisation by cooling kettle is provided with the right of separator, crystallisation by cooling kettle upper end connection evaporator lower end, crystallisation by cooling kettle lower end connects centrifuge, crystallisation by cooling kettle lower right is provided with recovery acid tank, acid tank is reclaimed to be connected on centrifuge.
Description
Technical field
The invention belongs to spent acid processing technology field, and in particular to a kind of spent acid single effect evaporation processing unit
Background technology
Acid is in the industry extensive use such as chemical industry, steel.In many production processes, sour utilization rate is very low, substantial amounts of acid
Emitted in company with acid-bearing wastewater.These waste water are such as discharged into environment without processing, can not only make water body or soil acid
Change, ecological environment is caused harm, and waste ample resources.Spent acid and acid waste water are in addition to acidity, also containing a large amount of
Impurity.Harm of the spent acid to underground water is much larger than general wastewater from chemical industry.Specifically, spent acid is while permeating the ground,
River or underground are included by the heavy metal in rock, soil is reacted, severe contamination is caused to river or underground water;Also with rock
Sulphite, sulfide reaction in soil release the pernicious gas such as sulfur dioxide and hydrogen sulfide.If in addition, spent acid is not using conforming to
Reason, for producing the fertilizer type product such as phosphate fertilizer, ammonium sulfate, magnesium sulfate, organic fertilizer, nuisance will enter soil with fertilizer, cause
Organic pollution of soil;Irrigated with the water polluted by spent acid, can cause soil acidification, heavy metal in acid soil activity compared with
Height, is easily absorbed by plants, food-safe to cause major hidden danger.
The content of the invention
It is an object of the invention to provide a kind of spent acid single effect evaporation processing unit, solve present in such scheme not
Foot.
In order to achieve the above object, the technical solution used in the present invention is:
A kind of spent acid single effect evaporation processing unit, mainly by spent acid groove, filter, evaporator, separator, crystallisation by cooling
Kettle, centrifuge, recovery acid tank, condenser, recovery tank, vacuum buffer tank and vacuum pump assembly composition, described filter are set
Put on the right of spent acid groove, filter upper right side is provided with separator, the separator upper left corner is connected with filter, and the separator left side is set
There is evaporator and be connected with each other with separator, crystallisation by cooling kettle, crystallisation by cooling kettle upper end connection evaporator are provided with the right of separator
Reclaim acid tank provided with acid tank is reclaimed and be connected to centrifugation in lower end, crystallisation by cooling kettle lower end connection centrifuge, crystallisation by cooling kettle lower right
On machine, reclaim and condenser is provided with the acid tank upper right corner, condenser top is connected with separator, and recycle-water is provided with the downside of condenser
Groove, reclaims and vacuum buffer tank is provided with the right of tank, and vacuum buffer tank is connected with reclaiming tank, and the vacuum buffer tank lower right corner is provided with
Positive sky pump assembly.
The described crystallisation by cooling kettle lower left corner is provided with cooling water inlet, and the crystallisation by cooling kettle upper right corner is provided with coolant outlet.
The present invention reduces former process costs, the former process costs of pickling quality, reduction is not influenceed, pickling quality is not influenceed, real
The continuity of production is showed.Reduce potential safety hazard when spent acid processing and accumulating.Remove contained oil, wax, fat etc. in pickle
Organic impurities, it is ensured that the quality of surface treatment.Significantly reduce environmental pollution.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention;
1- spent acid grooves;2- filters;3- evaporators;4- separators;5- crystallisation by cooling kettles;6- centrifuges;7- reclaims acid tank;
8- condensers;9- reclaims tank;10- vacuum buffer tanks;11- vacuum pump assemblys.
Embodiment
The present invention is further described with reference to the accompanying drawings and detailed description.
As shown in figure 1, a kind of spent acid single effect evaporation processing unit, mainly by spent acid groove 1, filter 2, evaporator 3, separation
Device 4, crystallisation by cooling kettle 5, centrifuge 6, recovery acid tank 7, condenser 8, recovery tank 9, vacuum buffer tank 10 and vacuum pump assembly
11 compositions, described filter 2 is arranged on the right of spent acid groove 1, and the upper right side of filter 2 is provided with separator 4, the upper left corner of separator 4
It is connected with filter 2, the left side of separator 4 is connected with each other provided with evaporator 3 and with separator 4, the right of separator 4 is provided with cooling
Crystallization kettle 5, the upper end of crystallisation by cooling kettle 5 connection evaporator 3 lower end, the lower end of crystallisation by cooling kettle 5 connection centrifuge 6, crystallisation by cooling kettle 5
Lower right is reclaimed acid tank 7 and is connected on centrifuge 6 provided with acid tank 7 is reclaimed, and reclaims and condenser 8 is provided with the upper right corner of acid tank 7, cold
The top of condenser 8 is connected with separator 4, and the downside of condenser 8 reclaims the right of tank 9 and be provided with vacuum buffer tank provided with tank 9 is reclaimed
10, vacuum buffer tank 10 is connected with reclaiming tank 9, and the lower right corner of vacuum buffer tank 10 is provided with positive empty pump assembly 11;Described is cold
But the lower left corner of crystallization kettle 5 is provided with cooling water inlet, and the crystallisation by cooling kettle upper right corner is provided with coolant outlet.
Claims (3)
1. a kind of spent acid single effect evaporation processing unit, by spent acid groove, filter, evaporator, separator, crystallisation by cooling kettle, centrifugation
Machine, recovery acid tank, condenser, recovery tank, vacuum buffer tank and vacuum pump assembly composition, it is characterised in that:Described filtering
Device is arranged on the right of spent acid groove, and filter upper right side is provided with separator, and the separator upper left corner is connected with filter, and separator is left
Side is connected with each other provided with evaporator and with separator, and crystallisation by cooling kettle is provided with the right of separator, and the connection of crystallisation by cooling kettle upper end is steamed
Device lower end is sent out, crystallisation by cooling kettle lower end connection centrifuge, crystallisation by cooling kettle lower right is reclaimed acid tank and be connected to provided with acid tank is reclaimed
On centrifuge, reclaim and condenser is provided with the acid tank upper right corner, condenser top is connected with separator, is provided with back on the downside of condenser
Tank is received, reclaims and vacuum buffer tank is provided with the right of tank, vacuum buffer tank is connected with reclaiming tank, the vacuum buffer tank lower right corner
Provided with positive empty pump assembly.
2. spent acid single effect evaporation processing unit according to claim 1, it is characterised in that:Described crystallisation by cooling kettle lower-left
Angle is provided with cooling water inlet.
3. spent acid single effect evaporation processing unit according to claim 1, it is characterised in that:The crystallisation by cooling kettle upper right corner is provided with
Coolant outlet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710567359.0A CN107140780A (en) | 2017-07-12 | 2017-07-12 | A kind of spent acid single effect evaporation processing unit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710567359.0A CN107140780A (en) | 2017-07-12 | 2017-07-12 | A kind of spent acid single effect evaporation processing unit |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107140780A true CN107140780A (en) | 2017-09-08 |
Family
ID=59776202
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710567359.0A Withdrawn CN107140780A (en) | 2017-07-12 | 2017-07-12 | A kind of spent acid single effect evaporation processing unit |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107140780A (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20110036471A (en) * | 2009-10-01 | 2011-04-07 | 김기원 | A toxic substance waste lime disposal method |
CN202072465U (en) * | 2011-05-24 | 2011-12-14 | 钱钧 | Pickling waste liquid recycling treatment device |
CN205442933U (en) * | 2016-03-17 | 2016-08-10 | 常州市风华环保有限公司 | Spent acid processing apparatus |
CN206915927U (en) * | 2017-07-12 | 2018-01-23 | 苏州艾特斯环保材料有限公司 | A kind of spent acid single effect evaporation processing unit |
CN108147471A (en) * | 2018-01-02 | 2018-06-12 | 张家港洁利环保科技有限公司 | The industrial process of Feromax crystal |
-
2017
- 2017-07-12 CN CN201710567359.0A patent/CN107140780A/en not_active Withdrawn
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20110036471A (en) * | 2009-10-01 | 2011-04-07 | 김기원 | A toxic substance waste lime disposal method |
CN202072465U (en) * | 2011-05-24 | 2011-12-14 | 钱钧 | Pickling waste liquid recycling treatment device |
CN205442933U (en) * | 2016-03-17 | 2016-08-10 | 常州市风华环保有限公司 | Spent acid processing apparatus |
CN206915927U (en) * | 2017-07-12 | 2018-01-23 | 苏州艾特斯环保材料有限公司 | A kind of spent acid single effect evaporation processing unit |
CN108147471A (en) * | 2018-01-02 | 2018-06-12 | 张家港洁利环保科技有限公司 | The industrial process of Feromax crystal |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN203170696U (en) | Leaching and repairing equipment of polluted soil | |
CN105480988B (en) | A kind of method that high-purity ammonium salt is prepared from impurity ammonium salt waste liquid high | |
CN204079685U (en) | A kind for the treatment of unit of high salinity high-COD waste water | |
CN102502709A (en) | Method for extracting secondary salt from coking desulphurized waste liquid | |
CN103787542B (en) | The wastewater recovery processing technique that a kind of Preparation of Sebacic Acid From Castor Oil produces and device | |
CN102616765A (en) | Method of using composite extracting agent for extraction and refining of phosphoric acid prepared through wet process | |
CN207175684U (en) | The system that hydrochloric acid and metallic compound are reclaimed from hydrochloric acid pickling waste liquor | |
CN103073145A (en) | System for recovering light oil from residual ammonia water | |
CN101967033A (en) | Decrement, resource protection and innocent treatment method for tank bottom oil sludge | |
CN104787946B (en) | A kind of wholly-owned source utilization process of steel rolling spent acid | |
CN206915927U (en) | A kind of spent acid single effect evaporation processing unit | |
CN208829280U (en) | A kind of polycrystalline silicon slurry high efficiente callback process system | |
CN113979568A (en) | Arsenic removal treatment process for high-arsenic-content strong-acid wastewater | |
CN104232133B (en) | Potassium, the method and device of sodium ions content in a kind of reduction coal tar | |
CN107140780A (en) | A kind of spent acid single effect evaporation processing unit | |
CN212282979U (en) | Efficient crude phenol extraction device | |
CN207108731U (en) | Aluminum profile extrusion wastewater treatment equipment | |
CN102874848A (en) | Method for recovering sodium bicarbonate and organic acid sodium salt from cyclohexanone waste alkali solution | |
CN204897624U (en) | Sulphur ammonium waste water comprehensive control retrieval and utilization device is smelted to tombarthite | |
CN101362607A (en) | Process for treating waste water from hexane diacid production system | |
CN102936063B (en) | Process method and system for recovering water from lignite drying flue gas | |
CN204174288U (en) | A kind of ion film caustic soda production equipment improving bittern usage ratio | |
CN102676813B (en) | New process for treating interphase dirt produced by P204 extraction system | |
CN203319810U (en) | High-concentration hydrometallurgy wastewater circulating recovery emission reduction system | |
CN107129087A (en) | A kind of refuse leachate deamination removes chromium process method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20170908 |
|
WW01 | Invention patent application withdrawn after publication |