CN207101931U - A kind of anticorrosive paint production enrichment facility - Google Patents
A kind of anticorrosive paint production enrichment facility Download PDFInfo
- Publication number
- CN207101931U CN207101931U CN201720493746.XU CN201720493746U CN207101931U CN 207101931 U CN207101931 U CN 207101931U CN 201720493746 U CN201720493746 U CN 201720493746U CN 207101931 U CN207101931 U CN 207101931U
- Authority
- CN
- China
- Prior art keywords
- cleaning fluid
- enrichment facility
- anticorrosive paint
- shower
- kettle
- 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.)
- Expired - Fee Related
Links
Landscapes
- Cleaning By Liquid Or Steam (AREA)
Abstract
A kind of anticorrosive paint production enrichment facility described in the utility model, it includes material kettle, vaporization chamber, agitator, motor, vaporization cycle pipe, evaporative recirculation pump, cleaning liquid storage tank, cleaning fluid circulating pump, cleaning fluid circulation pipe, cleaning fluid recovery storage tank, condenser, vavuum pump.Agitator, the motor connection that agitator is externally provided with material bottom portion are provided with inside described material kettle;The utility model effectively improves that material is rapidly heated and thermally equivalent avoids fouling by using agitator in material kettle and chuck heating design;The rotary spray head design being provided with simultaneously using cleaning shower, " plugging " and " incrustation " phenomenon that timely and effective can be handled falling film evaporation pipe and occur, improves thickening efficiency;The utility model also have it is rational in infrastructure, it is ingenious in design, it is easy to operate the advantages of.
Description
Technical field
The utility model belongs to chemical industry equipment, and in particular to a kind of anticorrosive paint production enrichment facility.
Background technology
In order to prevent plant equipment to be damaged in being worked under acid or alkaline environment by corrosion, corrosion-resistant processing most convenient
One of mode be exactly directly in plant equipment surface or engineering construction surface spraying anticorrosive paint.
Enrichment facility is usually to add feed liquid from falling film evaporator heating chamber upper tube box, is filled through liquid distribution and film forming
Put, be evenly distributed in each heat exchanger tube, under gravity and vacuum induced and airflow function, flowed from top to bottom into uniformly membranaceous,
Gas-liquid is sufficiently separated, and obtains concentrate.Be widely used in medicine, food, chemical industry, etc. industry water or organic solution evaporation it is dense
Contracting, and with evaporability is high, energy-saving, operating cost is low and can guarantee that material consistency in evaporation process.In anti-corrosion
In coating material production preparation process, concentration and evaporation is carried out using enrichment facility, so as to reach certain density material, is made for a long time
It is adhered to precipitum afterwards, is often had on evaporating heat-exchanging pipe, so as to influence heat exchange efficiency.
The content of the invention
Goal of the invention:The purpose of this utility model is to overcome deficiency of the prior art, there is provided a kind of structure design
Rationally, the high anticorrosive paint production enrichment facility of evaporation efficiency, its is easy to operate, and practicality is high.
Technical scheme:In order to solve the above-mentioned technical problem, a kind of anticorrosive paint production concentration described in the utility model
Device, it includes material kettle, vaporization chamber, agitator, motor, vaporization cycle pipe, evaporative recirculation pump, cleaning liquid storage tank, cleaning fluid
Circulating pump, cleaning fluid circulation pipe, cleaning fluid recovery storage tank, condenser, vavuum pump.Agitator is provided with inside described material kettle,
The motor connection that agitator is externally provided with material bottom portion;The material kettle top is provided with vaporization chamber, if evaporation chamber is provided with
Dry group falling film evaporation pipe;The outer side of the material kettle is provided with vaporization cycle pipe, evaporative recirculation pump, material shower and forms evaporation and follow
Ring;Described material shower is provided with spray head;The outer opposite side of the material kettle be provided with cleaning liquid storage tank, cleaning fluid circulating pump,
Cleaning fluid circulation pipe, cleaning fluid recovery storage tank, cleaning fluid shower form clean cycle;Described cleaning fluid shower is provided with rotation
Turn spray head;It is connected at the top of described vaporization chamber by pipeline with condenser, condenser is connected by pipeline with vavuum pump.
Described agitator is gate stirrer.
Described material kettle top is provided with material charging aperture and temperature measuring set.
Material sample tap is provided with the middle part of described material kettle.
Described material bottom portion is provided with concentrate drain hole.
Described material kettle is externally provided with chuck, and chuck upper wall portions are provided with steam inlet, and chuck lower wall portion is provided with steam drainage
Mouthful.
Described vaporization chamber upper wall portions are provided with steam inlet, and vaporization chamber lower wall portion is provided with steam drainage mouth.
Beneficial effect:Compared with prior art, its remarkable advantage is the utility model:The utility model is by using material
Agitator and chuck heating design in kettle, effectively improve material and be rapidly heated and thermally equivalent, avoid coking;Simultaneously using cleaning
The rotary spray head design that shower is provided with, it is existing timely and effective can to handle " plugging " and " incrustation " that falling film evaporation pipe occurs
As improving thickening efficiency;The utility model also have it is rational in infrastructure, it is ingenious in design, it is easy to operate the advantages of.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present utility model.
Embodiment
The utility model is further described with reference to the accompanying drawings and examples.
As shown in figure 1, a kind of anticorrosive paint production enrichment facility described in the utility model, it includes material kettle 1, steamed
Send out room 2, agitator 3, motor 4, falling film evaporation pipe 5;Vaporization cycle pipe 6, evaporative recirculation pump 7, cleaning liquid storage tank 8, cleaning fluid follow
Ring pump 9, cleaning fluid circulation pipe 10, cleaning fluid recovery storage tank 11, condenser 12, vavuum pump 13.The described inside of material kettle 1 is provided with
Agitator 3, the motor 4 that agitator 3 is externally provided with the bottom of material kettle 1 are connected;The top of material kettle 1 is provided with vaporization chamber 2, evaporation
The inside of room 2 is provided with some groups of falling film evaporation pipes 5;The 1 outer side of material kettle is provided with vaporization cycle pipe 6, evaporative recirculation pump 7, thing
Expect that shower 14 forms vaporization cycle;Described material shower 14 is arranged on the top of falling film evaporation pipe 5, and material shower 14 is set
There is spray head 15;The 1 outer opposite side of material kettle is provided with cleaning liquid storage tank 8, cleaning fluid circulating pump 9, cleaning fluid circulation pipe 10, clear
Washing lotion recovery storage tank 11, cleaning fluid shower 16 form clean cycle;Described cleaning fluid shower 16 is arranged in vaporization chamber 2
The top of material shower 14, cleaning fluid shower 16 are provided with rotary spray first 17;The top of described vaporization chamber 2 by pipeline with
Condenser 12 is connected, and condenser 12 is connected by pipeline with vavuum pump 13.
Described agitator 3 is gate stirrer.
The described top of material kettle 1 is provided with material charging aperture 18 and temperature measuring set 19.
The middle part of material kettle 1 is provided with material sample tap 20.
The described bottom of material kettle 1 is provided with concentrate drain hole 21.
Described material kettle 1 is externally provided with chuck 22, and the upper wall portions of chuck 22 are provided with steam inlet 23, and the lower wall portion of chuck 22 is provided with
Steam drainage mouth 24.
The described upper wall portions of vaporization chamber 2 are provided with steam inlet 25, and the lower wall portion of vaporization chamber 2 is provided with steam drainage mouth 26.
The described outlet of evaporative recirculation pump 7 by vaporization cycle pipe 6 and material shower 14 connect, evaporative recirculation pump 7
Import is connected by vaporization cycle pipe 6 with the bottom of material kettle 1.
The described import of cleaning fluid circulating pump 9 is connected by cleaning fluid circulation pipe 10 with cleaning liquid storage tank 8;Cleaning fluid circulates
The outlet of pump 9 is connected by cleaning fluid circulation pipe 10 with cleaning fluid shower 16, the cleaning fluid circulation pipe 10 of the bottom of connection material kettle 1
It is provided with threeway connection cleaning fluid recovery storage tank 11;It is repeatable to recycle after cleaning fluid recycling.
The utility model provides a kind of thinking and method, and it is many to implement method and the approach of the technical scheme, with
Only it is preferred embodiment of the present utility model described in upper, it is noted that for those skilled in the art,
On the premise of the utility model principle is not departed from, some improvements and modifications can also be made, these improvements and modifications should also regard
For the scope of protection of the utility model, the available prior art of each part being not known in the present embodiment is realized.
Claims (9)
- A kind of 1. anticorrosive paint production enrichment facility, it is characterised in that described enrichment facility it include material kettle (1), steam Send out room (2), agitator (3), motor (4), falling film evaporation pipe (5);Vaporization cycle pipe (6), evaporative recirculation pump (7), cleaning fluid storage Tank (8), cleaning fluid circulating pump (9), cleaning fluid circulation pipe (10), cleaning fluid recovery storage tank (11), condenser (12), vavuum pump (13);Agitator (3), the motor (4) that agitator (3) is externally provided with material kettle (1) bottom are provided with inside described material kettle (1) Connection;Material kettle (1) top is provided with vaporization chamber (2), and some groups of falling film evaporation pipes (5) are provided with inside vaporization chamber (2);It is described Material kettle (1) outer side is provided with vaporization cycle pipe (6), evaporative recirculation pump (7), material shower (14) and forms vaporization cycle;Institute The material shower (14) stated is arranged on above falling film evaporation pipe (5), and material shower (14) is provided with spray head (15);The thing Expect that kettle (1) outer opposite side is provided with cleaning liquid storage tank (8), cleaning fluid circulating pump (9), cleaning fluid circulation pipe (10), cleaning fluid recovery Storage tank (11), cleaning fluid shower (16) form clean cycle;Described cleaning fluid shower (16) is arranged in vaporization chamber (2) The top of material shower (14), cleaning fluid shower (16) are provided with rotary spray head (17);It is logical at the top of described vaporization chamber (2) Piping is connected with condenser (12), and condenser (12) is connected by pipeline with vavuum pump (13).
- A kind of 2. anticorrosive paint production enrichment facility according to claim 1, it is characterised in that described agitator (3) it is gate stirrer.
- A kind of 3. anticorrosive paint production enrichment facility according to claim 1, it is characterised in that described material kettle (1) top is provided with material charging aperture (18) and temperature measuring set (19).
- 4. a kind of anticorrosive paint production enrichment facility according to claim 1, it is characterised in that in the middle part of material kettle (1) Provided with material sample tap (20).
- A kind of 5. anticorrosive paint production enrichment facility according to claim 1, it is characterised in that described material kettle (1) bottom is provided with concentrate drain hole (21).
- A kind of 6. anticorrosive paint production enrichment facility according to claim 1, it is characterised in that described material kettle (1) chuck (22) is externally provided with, chuck (22) upper wall portions are provided with steam inlet (23), and chuck (22) lower wall portion is provided with steam drainage mouth (24)。
- A kind of 7. anticorrosive paint production enrichment facility according to claim 1, it is characterised in that described vaporization chamber (2) upper wall portions are provided with steam inlet (25), and vaporization chamber (2) lower wall portion is provided with steam drainage mouth (26).
- A kind of 8. anticorrosive paint production enrichment facility according to claim 1, it is characterised in that described vaporization cycle Pump (7) outlet by vaporization cycle pipe (6) and material shower (14) connect, evaporative recirculation pump (7) import by evaporation follow Endless tube (6) is connected with material kettle (1) bottom.
- 9. a kind of anticorrosive paint production enrichment facility according to claim 1, it is characterised in that described cleaning fluid follows (9) import of ring pump is connected by cleaning fluid circulation pipe (10) with cleaning liquid storage tank (8);Cleaning fluid circulating pump (9) outlet passes through clear Washing lotion circulation pipe (10) is connected with cleaning fluid shower (16), is connected and is set on the cleaning fluid circulation pipe (10) of material kettle (1) bottom There is threeway connection cleaning fluid recovery storage tank (11).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720493746.XU CN207101931U (en) | 2017-05-05 | 2017-05-05 | A kind of anticorrosive paint production enrichment facility |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720493746.XU CN207101931U (en) | 2017-05-05 | 2017-05-05 | A kind of anticorrosive paint production enrichment facility |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207101931U true CN207101931U (en) | 2018-03-16 |
Family
ID=61594327
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720493746.XU Expired - Fee Related CN207101931U (en) | 2017-05-05 | 2017-05-05 | A kind of anticorrosive paint production enrichment facility |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207101931U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106924983A (en) * | 2017-05-05 | 2017-07-07 | 江苏格桑花涂料有限公司 | A kind of anticorrosive paint production enrichment facility |
-
2017
- 2017-05-05 CN CN201720493746.XU patent/CN207101931U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106924983A (en) * | 2017-05-05 | 2017-07-07 | 江苏格桑花涂料有限公司 | A kind of anticorrosive paint production enrichment facility |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106924983A (en) | A kind of anticorrosive paint production enrichment facility | |
CN204329716U (en) | A kind of heat exchanger circulation apparatus for eliminating sludge | |
CN204421406U (en) | A kind of automatically descaling solar water heater | |
CN206094974U (en) | Waste water waste heat recovery device | |
CN208139875U (en) | A kind of cooling tower being equipped with hydrophilic filler board group part | |
CN211169934U (en) | Miniature evaporation crystallization equipment | |
CN207101931U (en) | A kind of anticorrosive paint production enrichment facility | |
CN102519300A (en) | Method for chemically and circularly cleaning scale inside and outside pipes of evaporating tank and heater in the sugar factory | |
CN209500800U (en) | A kind of forced circulation MVR evaporator | |
CN206437913U (en) | A kind of cooling water chemicals dosing plant for recirculating cooling water system | |
CN205393114U (en) | Level pipe falling film evaporation ware belt cleaning device | |
CN208104553U (en) | A kind of chemically-cleaning device of low-temperature multi-effect seawater desalination device | |
CN108159717B (en) | Internal rotation heating circulation evaporator and system for treating salt-containing wastewater by using same | |
CN206235235U (en) | A kind of coil heat exchanger cleaning device | |
CN209166192U (en) | A kind of starch-based product production plate heat exchanger structure | |
CN208193698U (en) | Inward turning heat cycles evaporator and its system for handling brine waste | |
CN203899171U (en) | Novel waste heat/live steam compound evaporator | |
CN208952067U (en) | A kind of device using oxygen-eliminating device oxygen discharging door exhaust gas heating boiler feed water | |
CN207153133U (en) | A kind of falling film evaporator | |
CN207237310U (en) | High concentration inspissator | |
CN206355613U (en) | One kind weaving terylene finishing agent production falling film evaporator | |
CN205773473U (en) | A kind of brine waste spray evaporation processing system | |
CN206642385U (en) | Multiple-effect falling film is evaporated in vacuo condenser apparatus | |
CN205759824U (en) | Descaling and antiscaling MVR mechanical compress evaporated crystallization device | |
CN205761103U (en) | A kind of dilute sulfuric acid concentration glassed steel reaction vessels |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180316 Termination date: 20190505 |
|
CF01 | Termination of patent right due to non-payment of annual fee |