CN205031912U - Titanium material triple effect evaporation plant - Google Patents
Titanium material triple effect evaporation plant Download PDFInfo
- Publication number
- CN205031912U CN205031912U CN201520748065.4U CN201520748065U CN205031912U CN 205031912 U CN205031912 U CN 205031912U CN 201520748065 U CN201520748065 U CN 201520748065U CN 205031912 U CN205031912 U CN 205031912U
- Authority
- CN
- China
- Prior art keywords
- effect
- triple
- degree
- vaporization system
- heat exchanger
- 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
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a titanium material triple effect evaporation plant, it includes an effect vaporization system, two effect vaporization system and the triple effect vaporization system that connect gradually with the series system, one of them is imitated between vaporization system and the two effect vaporization system and passes through the flash steam pipe connection between two effect vaporization system and the triple effect vaporization system, an effect vaporization system, two effect vaporization system and triple effect vaporization system equally divide and do not include evaporimeter, axial compressor circulating pump and heat exchanger, and wherein the entrance point of axial compressor circulating pump is provided with pump import tapered pipe, and the exit end of axial compressor circulating pump is provided with and pumps a mouthful tapered pipe, evaporation plant adopts the preparation of titanium material, has still set up 90 degrees return bends, expansion joint, takeover isotructure among the vaporization system, makes complete equipment compact structure, reasonable, has improved production efficiency greatly, has compensatied the defect of current social production quantity not sufficient effectively.
Description
Technical field
The utility model relates to a kind of vaporising device, is specifically related to a kind of rational in infrastructure, service efficiency is high, output is large titanium material triple-effect evaporation plant.
Background technology
Evaporation is one of important unit operations of modern chemical industry, namely utilizes the method for heating to make the partial solvent in solution vaporize and remove, to improve the concentration of solution or to create conditions for the precipitation of solute.At present, evaporation concentration device in each large field application such as Chemical Manufacture, food manufacturing, Sewage treatment, medicine processing widely, but existing various evaporation concentration device is generally single effect evaporation and concentrates, wherein water vapour can take away a large amount of evaporated liquor in the process of evaporation, can only produce by the natural coagulation of water vapour at device top the mode refluxed to reclaim the raw material run off along with water vapour, and the evaporated liquor raw material of the overwhelming majority runs off with water vapour, therefore, both caused serious wastage of material, discharge also pollutes the environment arbitrarily simultaneously.Although triple effect evaporator can partial rcsponse the problems referred to above, the various triple effect evaporators existed at present still have the defects such as efficiency is low, output is little and are badly in need of solving.
Utility model content
The purpose of this utility model is exactly for above-mentioned deficiency of the prior art, provides a kind of rational in infrastructure, service efficiency is high, output is large titanium material triple-effect evaporation plant.
To achieve these goals, the technical solution of the utility model is as described below:
Titanium material triple-effect evaporation plant, it comprises the effect vapo(u)rization system, two effect vapo(u)rization system and the triple effect evaporation systems that connect successively in a series arrangement, wherein, a described effect vapo(u)rization system comprises 1st effective evaporator, axial flow circulating pump and an effect heat exchanger, described two effect vapo(u)rization systems comprise 2nd effect evaporator, axial flow circulating pump and two effect heat exchangers, described triple effect evaporation system comprises triple effect evaporator, axial flow circulating pump and three-effect heat exchanger, the entrance point of described axial flow circulating pump is provided with pump inlet reduced pipe, and the port of export of described axial flow circulating pump is provided with pump discharge reduced pipe.
Preferably, a described effect vapo(u)rization system and described two to be imitated between vapo(u)rization system and described two is imitated between vapo(u)rization system with described triple effect evaporation system and be connected by indirect steam pipeline.
Preferably, the top of described 1st effective evaporator, 2nd effect evaporator and triple effect evaporator is provided with demister.
Preferably, in a described effect vapo(u)rization system, 1st effective evaporator lower end is provided with adapter, described adapter is connected with pump inlet reduced pipe by expansion joint, described pump discharge reduced pipe is connected with the one 90 degree of bend pipe, described one 90 degree of bend pipe is imitated heat exchanger by expansion joint and and is connected, and a described effect heat exchanger is connected with 1st effective evaporator by the 2 90 degree of bend pipe.
Preferably, in described two effect vapo(u)rization systems, 2nd effect evaporator lower end is provided with adapter, described adapter is connected with pump inlet reduced pipe by expansion joint, described pump discharge reduced pipe is connected with the one 90 degree of bend pipe, described one 90 degree of bend pipe is imitated heat exchanger by expansion joint and two and is connected, and described two effect heat exchangers are connected with 2nd effect evaporator by the 2 90 degree of bend pipe.
Preferably, in described triple effect evaporation system, triple effect evaporator lower end is provided with the 3 90 degree of bend pipe, the lower end of described 3 90 degree of bend pipe is connected with adapter, described adapter is connected with pump inlet reduced pipe by expansion joint, described pump discharge reduced pipe is connected with the one 90 degree of bend pipe, and described one 90 degree of bend pipe is connected with three-effect heat exchanger by expansion joint, and described three-effect heat exchanger is connected with triple effect evaporator by the 2 90 degree of bend pipe.
Titanium material triple-effect evaporation plant provided by the utility model, wherein three boiling system is connected by indirect steam pipeline, and each vapo(u)rization system makes integrated connection compact, rationally distributed by arranging the various pipeline such as adapter, 90 degree of bend pipes; Meanwhile, the elastic expansion joint with free-extension function is set, functional, compact conformation at different pipeline junction; In addition, the entrance point of axial flow circulating pump arranges pump inlet reduced pipe, and the port of export arranges pump discharge reduced pipe, and three is with the use of reducing flow velocity, reduce hydraulic loss.
To sum up, the utility model adopts the preparation of titanium material and obtains, all parts material is all through well-chosen and design, overall structure is simply compact, therefore, compared with prior art, titanium material triple-effect evaporation plant provided by the utility model has the advantage that evaporation efficiency is high, output is large, can greatly make up the defect that in each field of prior art, vaporising device service efficiency is low, output is not enough.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
Fig. 1 is the structural representation of titanium material triple-effect evaporation plant in the utility model embodiment.
In figure: 1, demister; 2-1,1st effective evaporator; 2-2,2nd effect evaporator; 2-3, triple effect evaporator; 3, take over; 4, expansion joint; 5, pump inlet reduced pipe; 6, axial flow circulating pump; 7, pump discharge reduced pipe; 8-1, the one 90 degree of bend pipe; 8-2, the 2 90 degree of bend pipe; 8-3, the 3 90 degree of bend pipe; 9-1, an effect heat exchanger; 9-2, two effect heat exchangers; 9-3, triple effect evaporator; 10, indirect steam pipeline.
Detailed description of the invention
Below in conjunction with drawings and Examples, detailed description of the invention of the present utility model is described in further detail.Following examples for illustration of the utility model, but are not used for limiting scope of the present utility model.
As shown in Figure 1, a kind of titanium material triple-effect evaporation plant, it comprises the effect vapo(u)rization system connected successively in a series arrangement, two effect vapo(u)rization system and triple effect evaporation systems, wherein, a described effect vapo(u)rization system comprises 1st effective evaporator 2-1, axial flow circulating pump 6 and an effect heat exchanger 9-1, described two effect vapo(u)rization systems comprise 2nd effect evaporator 2-2, axial flow circulating pump 6 and two effect heat exchanger 9-2, described triple effect evaporation system comprises triple effect evaporator 2-3, axial flow circulating pump 6 and three-effect heat exchanger 9-3, the entrance point of described axial flow circulating pump 6 is provided with pump inlet reduced pipe 5, the port of export of described axial flow circulating pump 6 is provided with pump discharge reduced pipe 7,
A described effect vapo(u)rization system and described two to be imitated between vapo(u)rization system and described two is imitated between vapo(u)rization system with described triple effect evaporation system and be connected by indirect steam pipeline 10;
The top of described 1st effective evaporator 2-1,2nd effect evaporator 2-2 and triple effect evaporator 2-3 is provided with demister 1;
In a described effect vapo(u)rization system, 1st effective evaporator 2-1 lower end is provided with adapter 3, described adapter 3 is connected with pump inlet reduced pipe 5 by expansion joint 4, described pump discharge reduced pipe 7 is connected with the one 90 degree of bend pipe 8-1, described one 90 degree of bend pipe 8-1 is imitated heat exchanger 9-1 by expansion joint 4 and and is connected, and a described effect heat exchanger 9-1 is connected with 1st effective evaporator 2-1 by the 2 90 degree of bend pipe 8-2;
In described two effect vapo(u)rization systems, 2nd effect evaporator 2-2 lower end is provided with adapter 3, described adapter 3 is connected with pump inlet reduced pipe 5 by expansion joint 4, described pump discharge reduced pipe 7 is connected with the one 90 degree of bend pipe 8-1, described one 90 degree of bend pipe 8-1 is imitated heat exchanger 9-2 by expansion joint 4 and two and is connected, and described two effect heat exchanger 9-2 are connected with 2nd effect evaporator 2-2 by the 2 90 degree of bend pipe 8-2.
In described triple effect evaporation system, triple effect evaporator 2-3 lower end is provided with the 3 90 degree of bend pipe 8-3, the lower end of described 3 90 degree of bend pipe 8-3 is connected with adapter 3, described adapter 3 is connected with pump inlet reduced pipe 5 by expansion joint 4, described pump discharge reduced pipe 7 is connected with the one 90 degree of bend pipe 8-1, described one 90 degree of bend pipe 8-1 is connected with three-effect heat exchanger 9-3 by expansion joint 4, and described three-effect heat exchanger 9-3 is connected with triple effect evaporator 2-3 by the 2 90 degree of bend pipe 8-2.
The above-mentioned explanation of embodiment disclosed in the utility model; those skilled in the art are realized or uses the utility model; simultaneously; these are only the preferred embodiment of the utility model embodiment; not in order to limit the utility model embodiment; within all spirit in the utility model embodiment and principle, any amendment done, equivalent replacement, improvement etc., within the protection domain that all should be included in the utility model embodiment.
Claims (6)
1. titanium material triple-effect evaporation plant, it is characterized in that, comprise the effect vapo(u)rization system connected successively in a series arrangement, two effect vapo(u)rization system and triple effect evaporation systems, a described effect vapo(u)rization system comprises 1st effective evaporator (2-1), axial flow circulating pump (6) and effect heat exchanger (9-1), described two effect vapo(u)rization systems comprise 2nd effect evaporator (2-2), axial flow circulating pump (6) and two effects heat exchanger (9-2), described triple effect evaporation system comprises triple effect evaporator (2-3), axial flow circulating pump (6) and three-effect heat exchanger (9-3), the entrance point of described axial flow circulating pump (6) is provided with pump inlet reduced pipe (5), the port of export of described axial flow circulating pump (6) is provided with pump discharge reduced pipe (7).
2. titanium material triple-effect evaporation plant according to claim 1, it is characterized in that, a described effect vapo(u)rization system and described two imitate between vapo(u)rization system and described two is imitated and pass through indirect steam pipeline (10) between vapo(u)rization system with described triple effect evaporation system and be connected.
3. titanium material triple-effect evaporation plant according to claim 2, it is characterized in that, the top of described 1st effective evaporator (2-1), 2nd effect evaporator (2-2) and triple effect evaporator (2-3) is provided with demister (1).
4. according to claim 1, titanium material triple-effect evaporation plant described in 2 or 3, it is characterized in that, in a described effect vapo(u)rization system, 1st effective evaporator (2-1) lower end is provided with adapter (3), described adapter (3) is connected with pump inlet reduced pipe (5) by expansion joint (4), described pump discharge reduced pipe (7) is connected with the one 90 degree of bend pipe (8-1), described one 90 degree of bend pipe (8-1) imitates heat exchanger (9-1) by expansion joint (4) and and is connected, described effect heat exchanger (9-1) is connected with 1st effective evaporator (2-1) by the 2 90 degree of bend pipe (8-2).
5. according to claim 1, titanium material triple-effect evaporation plant described in 2 or 3, it is characterized in that, in described two effect vapo(u)rization systems, 2nd effect evaporator (2-2) lower end is provided with adapter (3), described adapter (3) is connected with pump inlet reduced pipe (5) by expansion joint (4), described pump discharge reduced pipe (7) is connected with the one 90 degree of bend pipe (8-1), described one 90 degree of bend pipe (8-1) imitates heat exchanger (9-2) by expansion joint (4) and two and is connected, described two effects heat exchanger (9-2) are connected with 2nd effect evaporator (2-2) by the 2 90 degree of bend pipe (8-2).
6. according to claim 1, titanium material triple-effect evaporation plant described in 2 or 3, it is characterized in that, in described triple effect evaporation system, triple effect evaporator (2-3) lower end is provided with the 3 90 degree of bend pipe (8-3), the lower end of described 3 90 degree of bend pipe (8-3) is connected with adapter (3), described adapter (3) is connected with pump inlet reduced pipe (5) by expansion joint (4), described pump discharge reduced pipe (7) is connected with the one 90 degree of bend pipe (8-1), described one 90 degree of bend pipe (8-1) is connected with three-effect heat exchanger (9-3) by expansion joint (4), described three-effect heat exchanger (9-3) is connected with triple effect evaporator (2-3) by the 2 90 degree of bend pipe (8-2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520748065.4U CN205031912U (en) | 2015-09-24 | 2015-09-24 | Titanium material triple effect evaporation plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520748065.4U CN205031912U (en) | 2015-09-24 | 2015-09-24 | Titanium material triple effect evaporation plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205031912U true CN205031912U (en) | 2016-02-17 |
Family
ID=55290846
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520748065.4U Expired - Fee Related CN205031912U (en) | 2015-09-24 | 2015-09-24 | Titanium material triple effect evaporation plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205031912U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110465107A (en) * | 2019-08-07 | 2019-11-19 | 浙江宣达环境科技股份有限公司 | A kind of enrichment facility and method of sulfate process titanium dioxide liquid |
-
2015
- 2015-09-24 CN CN201520748065.4U patent/CN205031912U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110465107A (en) * | 2019-08-07 | 2019-11-19 | 浙江宣达环境科技股份有限公司 | A kind of enrichment facility and method of sulfate process titanium dioxide liquid |
| CN110465107B (en) * | 2019-08-07 | 2023-12-22 | 浙江宣达环境科技股份有限公司 | Concentrating device and method for sulfuric acid process titanium white liquid |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204034294U (en) | The board-like forced-circulation evaporator of novel triple effect | |
| CN102329037B (en) | Low-temperature multi-effect evaporation seawater desalinization device and method for desalting seawater | |
| CN205031912U (en) | Titanium material triple effect evaporation plant | |
| CN102840769B (en) | Closed cycle seawater cooling system for PTA process unit | |
| CN104307196A (en) | Triple-effect concentrator | |
| CN202865204U (en) | Vapor recycling device for fatty acid workshop | |
| CN203507566U (en) | Multi-effect starch sugar evaporator | |
| CN105948327A (en) | Wastewater zero discharging treatment integrated equipment | |
| CN205740561U (en) | Open circulating water thermal power plant former water water source device | |
| CN202415306U (en) | Device for preparing water for injection by utilizing reverse osmosis and ultrafiltration combined membrane method | |
| CN205360638U (en) | A double effect evaporator for traditional chinese medicine is concentrated | |
| CN203916115U (en) | A kind of dirty alcohol distillation column | |
| CN202876397U (en) | Slurry vacuum concentration system | |
| CN2877825Y (en) | Multi-effect multi-course evaporation concentration apparatus | |
| CN208932997U (en) | Alumina producer live steam condensed water processing unit | |
| CN212491601U (en) | Concentration and evaporation equipment for gelatin production | |
| CN210736274U (en) | Membrane concentration device with balanced concentrated water pressure | |
| CN205138246U (en) | Multistage condensing system | |
| CN102908791B (en) | Slurry vacuum concentration system | |
| CN208182648U (en) | It a kind of quickening waste water evaporative desalination and reduces and steams salt exhaust system | |
| CN208448691U (en) | A kind of anhydrous sodium sulphate evaporated crystallization device | |
| CN203620279U (en) | Steam recycling system | |
| CN203731376U (en) | Steam condensate heat exchange system equipped with automatic medicine adding device | |
| CN205127443U (en) | Equipment of terminal steam of multistage flashing device and waste gas is collected in condensation | |
| CN205718071U (en) | A kind of source of sewage falling film type big temperature difference heat pump assembly |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| 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: 20160217 Termination date: 20200924 |