CN209123365U - Tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device - Google Patents

Tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device Download PDF

Info

Publication number
CN209123365U
CN209123365U CN201822064140.1U CN201822064140U CN209123365U CN 209123365 U CN209123365 U CN 209123365U CN 201822064140 U CN201822064140 U CN 201822064140U CN 209123365 U CN209123365 U CN 209123365U
Authority
CN
China
Prior art keywords
vertical type
type evaporator
gas
liquid separator
continuous evaporation
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.)
Active
Application number
CN201822064140.1U
Other languages
Chinese (zh)
Inventor
叶志松
韦建东
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHANGSHU NEW-TECH CHEMICALS Co Ltd
Original Assignee
CHANGSHU NEW-TECH CHEMICALS Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by CHANGSHU NEW-TECH CHEMICALS Co Ltd filed Critical CHANGSHU NEW-TECH CHEMICALS Co Ltd
Priority to CN201822064140.1U priority Critical patent/CN209123365U/en
Application granted granted Critical
Publication of CN209123365U publication Critical patent/CN209123365U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The utility model discloses a kind of tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device, including vertical type evaporator, the side at the top of the vertical type evaporator offers steam inlet tube, and bottom side is provided with steam return line;The top of the vertical type evaporator passes through the lower part connection of pipeline and gas-liquid separator, and the top of the gas-liquid separator has feed pipe, and the bottom of the gas-liquid separator has the first vertical discharge nozzle, the second discharge nozzle connection with the vertical type evaporator.By the above-mentioned means, the utility model can control disengaging reduction of feed volume, it can be achieved that tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation, and can automatically control, it is easy to operate;When using the utility model, residence time of material is about 1st/20th of original process in evaporation process, and product colour is greatly improved.

Description

Tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device
Technical field
The utility model relates to chemical production equipment fields, fill more particularly to a kind of tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation It sets.
Background technique
Tetrakis hydroxymetyl phosphonium sulfuric is a kind of novel, efficient, quick, environmentally friendly, compatible strong biocide, it have wide spectrum, The features such as low dosage, low ratio foamed, low toxicity, easily biological-degradable, has outstanding environmental performance compared with traditional biocide, it It is not continuously present in environment, is more advantageous to environmental protection.It or a kind of novel dyeing and finishing auxiliaries for textile, can be used as textile Fire retardant, washability is good, can improve dyestuff absorptivity and anti-shrink of wool etc..It environmentally friendly kills livestock as a new generation Agent, THPS in use, will not generate secondary pollution.THPS oil industry, paper industry, industrial cooling circulating water system and Other environmental protection industry (epi)s are used widely.
The evaporation of tetrakis hydroxymetyl phosphonium sulfuric aqueous solution, existing technique are to carry out interval evaporation, dilute object using 5000L evaporating kettle Material is evaporated after evaporating kettle is added, and cooling material is transferred out after steaming to the concentration needed, using such method, when evaporation Material residence time in kettle is very long, more than 8 hours, material color burn, and due to being intermittently operated, it can not achieve certainly Dynamic control, inefficient operation.
Utility model content
The utility model, can mainly solving the technical problems that provide a kind of tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device Realize tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation.
In order to solve the above technical problems, the technical solution that the utility model uses is:
A kind of tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device, including vertical type evaporator, the top of the vertical type evaporator are provided The side in portion, offers steam inlet tube, and bottom side is provided with steam return line;The top of the vertical type evaporator by pipeline with The top of the lower part connection of gas-liquid separator, the gas-liquid separator has feed pipe, and the bottom of the gas-liquid separator has The first vertical discharge nozzle, the second discharge nozzle connection with the vertical type evaporator.
In one preferred embodiment of the utility model, the top of the gas-liquid separator connects condenser.
In one preferred embodiment of the utility model, the vertical type evaporator has steam jacket, and steam is in the steaming It circulates in vapour collet.
In one preferred embodiment of the utility model, it is connected with out after first discharge nozzle and second discharge nozzle Material pump, the discharging pump connect product storage tank.
In one preferred embodiment of the utility model, several control valves are provided on first discharge nozzle.
The beneficial effects of the utility model are: the utility model tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device, control disengaging Reduction of feed volume, it can be achieved that tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation, and can automatically control, it is easy to operate;It is practical new using this When type, residence time of material is about 1st/20th of original process in evaporation process, and product colour is greatly improved.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of one preferred embodiment of the utility model;
The components in the drawings are labeled as follows: 1, vertical type evaporator, 11, steam inlet tube, 12, steam return line, and 13, second goes out Expects pipe, 2, gas-liquid separator, 21, feed pipe, the 22, first discharge nozzle, 23, control valve.
Specific embodiment
The preferred embodiment of the utility model is described in detail with reference to the accompanying drawing, so that the advantages of the utility model It can be easier to be readily appreciated by one skilled in the art with feature, to make the protection scope of the utility model apparent clear Define.
A kind of tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device, including vertical type evaporator 1, the top of the vertical type evaporator 1 Side, offer steam inlet tube 11, bottom side is provided with steam return line 12;The top of the vertical type evaporator 1 passes through pipe The top of the lower part connection in road and gas-liquid separator 2, the gas-liquid separator 2 has feed pipe 21, the gas-liquid separator 2 Bottom has the first vertical discharge nozzle 22,13 connection of the second discharge nozzle with the vertical type evaporator 1.The gas-liquid separator 2 top connects condenser.The vertical type evaporator 1 has steam jacket, and steam circulates in the steam jacket.Described Discharging pump is connected with after one discharge nozzle 22 and second discharge nozzle 13, the discharging pump connects product storage tank.Described first Several control valves 23 are provided on discharge nozzle 22.
The use process of the utility model: steam enters steam jacket by steam inlet tube 11, and dilute material passes through gas-liquid point Feed pipe 21 from 2 top of device is added, and the vapor that vertical type evaporator 1 evaporates enters condenser by gas-liquid separator 2 and condenses, After material concentration reaches requirement, after material converges from the first discharge nozzle 22 and the second discharge nozzle 13, pumped from vertical type evaporator 1 Bottom is driven into product storage tank, throws dilute material into simultaneously in evaporation process, and the feed rate of dilute material is 2 ~ 4 ton/hours, Break away the material after qualified concentration simultaneously again, the flow speed of discharging is 1 ~ 2 ton/hour, keeps liquid level in 1.5 ~ 2m, temperature It is 70 ~ 85 DEG C, vacuum degree is greater than 6.5KPa, and continuous evaporation can be realized.
The continuous evaporation of tetrakis hydroxymetyl phosphonium sulfuric can be realized using the utility model, and can be automatically controlled, operation letter Just;When using the utility model, residence time of material is about 1st/20th of original process in evaporation process, and product colour is by depth Yellow becomes faint yellow, is greatly improved.
In the description of the present invention, it should be noted that term " on ", "lower", "left", "right", "inner", "outside" etc. The orientation or positional relationship of instruction be based on the orientation or positional relationship shown in the drawings or the utility model product use when The orientation or positional relationship usually put, is merely for convenience of describing the present invention and simplifying the description, rather than instruction or dark Show that signified device or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as pair The limitation of the utility model.The above description is only the embodiments of the present invention, is not intended to limit the patent of the utility model Range, equivalent structure or equivalent flow shift made by using the description of the utility model and the drawings, or directly or Other related technical areas are used in indirectly, are also included in the patent protection scope of the utility model.

Claims (5)

1. a kind of tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device, which is characterized in that including vertical type evaporator, the vertical type evaporator Top side, offer steam inlet tube, bottom side is provided with steam return line;Pass through pipe at the top of the vertical type evaporator The top of the lower part connection in road and gas-liquid separator, the gas-liquid separator has feed pipe, the bottom of the gas-liquid separator The second discharge nozzle connection with the first vertical discharge nozzle, with the vertical type evaporator.
2. tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device according to claim 1, which is characterized in that the gas-liquid separator Top connect condenser.
3. tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device according to claim 1, which is characterized in that the vertical type evaporator With steam jacket, steam circulates in the steam jacket.
4. tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device according to claim 1, which is characterized in that first discharge nozzle Be connected with discharging pump after second discharge nozzle, the discharging pump connects product storage tank.
5. tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device according to claim 1, which is characterized in that in first discharging Several control valves are provided on pipe.
CN201822064140.1U 2018-12-10 2018-12-10 Tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device Active CN209123365U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201822064140.1U CN209123365U (en) 2018-12-10 2018-12-10 Tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201822064140.1U CN209123365U (en) 2018-12-10 2018-12-10 Tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device

Publications (1)

Publication Number Publication Date
CN209123365U true CN209123365U (en) 2019-07-19

Family

ID=67248561

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201822064140.1U Active CN209123365U (en) 2018-12-10 2018-12-10 Tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device

Country Status (1)

Country Link
CN (1) CN209123365U (en)

Similar Documents

Publication Publication Date Title
CN103613155B (en) Heat pipe-type low temperature two sea water desalting equipment
CN201587871U (en) Multi-stage vacuum distillation sea water desalinating device
WO2017107020A1 (en) Household solar seawater desalination apparatus
CN102631789A (en) Evaporation falling film concentration technique
CN209123365U (en) Tetrakis hydroxymetyl phosphonium sulfuric continuous evaporation device
CN201834781U (en) Single-stage vacuum distillation seawater desalination device
CN208869344U (en) A kind of multiple-effect evaporation concentration systems of brine waste
CN205241433U (en) High salt of single -action multi -chambered mechanical compression evaporating treatment / high organic matter waste water device
CN204848322U (en) High salt solution processing system
CN204138355U (en) Flow-reversing dual-purpose ammonia concentrating unit
CN104307196A (en) Triple-effect concentrator
CN201686513U (en) Steam afterheat utilization unit and system for vacuum device of sea water desalination system
CN208877938U (en) A kind of multiple-effect evaporation concentration systems
CN206680334U (en) The drying and other treatment device of concentrate after a kind of percolate evaporation
CN103185362A (en) Low-position straight heating machine
CN209128080U (en) The dephosphorization apparatus of tetramethylol chloride evaporation condensed water
CN205516541U (en) High concentration efficiency's vacuum scraper blade is concentrated jar
CN109851134A (en) A kind of Room-temperature low-pressure seawater desalination system based on injection cavitation technique
CN108862438A (en) A kind of multiple-effect evaporation concentration systems of brine waste
CN108516603A (en) A kind of saliferous process for treating acidic sewage and system
CN208193712U (en) Molecular distillation apparatus for high-melting-point material
CN209714349U (en) Trimethylolpropane tris imitates condensing crystallizing vapo(u)rization system
CN103086451A (en) Multi-effect evaporative sea water desalinating device with hybrid process
CN207622559U (en) Self-evaporating type steam condenser
CN204684685U (en) A kind of cryogenic vacuum Chinese medicinal concentration equipment

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant