CN208711665U - A kind of tetrabromobisphenol A synthesis procedure adds bromine device automatically - Google Patents

A kind of tetrabromobisphenol A synthesis procedure adds bromine device automatically Download PDF

Info

Publication number
CN208711665U
CN208711665U CN201820885833.4U CN201820885833U CN208711665U CN 208711665 U CN208711665 U CN 208711665U CN 201820885833 U CN201820885833 U CN 201820885833U CN 208711665 U CN208711665 U CN 208711665U
Authority
CN
China
Prior art keywords
bromine
feedback
tetrabromobisphenol
chilled brine
synthesis procedure
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
CN201820885833.4U
Other languages
Chinese (zh)
Inventor
方典科
李恩
魏志
潘立海
乔连昌
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.)
Shandong Jin Yi New Materials Co Ltd
Original Assignee
Shandong Jin Yi New Materials 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 Shandong Jin Yi New Materials Co Ltd filed Critical Shandong Jin Yi New Materials Co Ltd
Priority to CN201820885833.4U priority Critical patent/CN208711665U/en
Application granted granted Critical
Publication of CN208711665U publication Critical patent/CN208711665U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The utility model discloses a kind of tetrabromobisphenol A synthesis procedures to add bromine device automatically, it is related to chemical synthesis apparatus field, it feeds including bromine discharging device and with the control metering device that it is connected by pipeline into reaction unit, it is equipped with cooling device outside the reaction unit, further includes self-checking device.Realize realization Discrete control, according to the temperature automatic adjustment bromine amount of reaction kettle, simultaneously, control data and the feeding sequences such as brine flow plus bromine weight, guarantee that synthetic reaction is more steady, product purity is improved, and alleviates labor intensity of workers, improves the technical effect of the safety coefficient of production.

Description

A kind of tetrabromobisphenol A synthesis procedure adds bromine device automatically
Technical field
The utility model relates to tetrabromobisphenol A production fields more particularly to a kind of tetrabromobisphenol A synthesis procedure to add bromine automatically Device.
Background technique
Tetrabromobisphenol A (TBBPA) chemical name 4,4- isopropylidene-bis--(2,6- dibromophenol) are relatively common at present A kind of brominated flame retardant.As reactive flame retardant, it can be used for epoxy resin, polyurethane resin etc.;As additive flame retardant Agent can be used for polystyrene, SAN resin and ABS resin etc., these resins are widely used in producing printed circuit board, electronics filling The shell of envelope material, household electrical appliance and electronic product.As additive flame retardant, it is applied to polycarbonate, unsaturated-resin, gathers The thermoplastics such as styrene and part thermosetting plastic resin, to assign its anti-flammability.
A certain amount of chlorine is usually added in the catalytic reaction stages of tetrabromobisphenol A production synthesis at this stage in a kettle Benzene, then starting stirring, is added sulfuric acid, catalysts selective, the hydrogen peroxide diluted, adds bisphenol-A, then start to be added dropwise Bromine;It is passed through circulation brine ice cooling in reacting kettle jacketing, drips sustained response 1h after bromine, obtains reaction solution;
The synthesis procedure step of tetrabromobisphenol A is more, and raw material type is more, and influence factor is more, and the producer of domestic production at present is all Manual feeding operation, the operating condition of standard configuration are the indexs such as safety interlocking temperature, liquid level, manual control charging sequence and speed, It is opposite to smoothly achieve synthesis process, but in this about 6 hours or so synthesis time for adding, worker requires sense of responsibility high, It frequently walks about and watches thermograph, estimate temperature rise trend, adjustment hand valve frequency is higher.If operating half-hearted or making mistakes, just It is difficult to steadily complete the index of synthesis procedure, can not guarantee the purity of product, and security risk is difficult to eradicate.
Utility model content
The purpose of the utility model is to provide a kind of tetrabromobisphenol A synthesis procedures to add bromine device automatically, realizes Discrete control, According to the temperature automatic adjustment bromine amount of reaction kettle, meanwhile, data and the feeding sequence such as control brine flow plus bromine weight are protected Card synthetic reaction is more steady, and product purity is improved, and alleviates labor intensity of workers, improves the safety system of production Number.
To solve the above problems, the utility model discloses a kind of tetrabromobisphenol A synthesis procedures to add bromine device automatically, including It bromine discharging device and feeds with the control metering device that it is connected by pipeline into reaction unit, outside the reaction unit It further include self-checking device equipped with cooling device;Wherein the bromine discharging device include bromine measuring tank and with bromine measuring tank The main hand-operated valve of outlet;The control metering device includes hand-operated valve, stop valve and metering pump, the stop valve and metering pump string It is in parallel with hand-operated valve after connection;The reaction unit includes reaction kettle and the blender that is set to inside reaction kettle;The cooling Device includes chilled brine water inlet pipe and chilled brine return pipe, and the chilled brine return pipe is equipped with flowmeter and freezing salt Water back water pump.
Wherein the self-checking device receives the weight from bromine measuring tank and feeds back, the switch feedback from stop valve, Velocity feedback and pressure leakage detection feedback from metering pump, the frequency feedback from blender, the flow feedback from flowmeter, The temperature of operation feedback and chilled brine water inlet pipe, chilled brine return pipe and reaction kettle from chilled brine back water pump is anti- Feedback.
Wherein the self-checking device sends switch command to stop valve to metering pump transmission speed adjustment signal, right Chilled brine sends start stop command, sends blowing to the external world and reminds.
Further wherein, the chilled brine back water pump can be by long-range and on the spot control.
The utility model has the beneficial effects that:
By device disclosed by the utility model, mitigate labor intensity of workers, safety coefficient is improved, according to tetrabromobisphenol A Process characteristic, it is practical in conjunction with production, add bromine system, Discrete control, according to the temperature automatic adjustment of reaction kettle by automatically controlling Bromine amount, meanwhile, data and the feeding sequence such as control brine flow plus bromine weight guarantee that synthetic reaction is more steady, make tetrabromo Bisphenol-A fusing point is more stable, and purity is improved.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment Or attached drawing needed to be used in the description of the prior art is briefly described.It is clear that the accompanying drawings in the following description is this reality Without creative efforts, may be used also for those of ordinary skill in the art with novel some embodiments To obtain other drawings based on these drawings.
Fig. 1 is the overall structure diagram of the utility model;
In figure: 1. discharging devices;2. controlling metering device;3. reaction unit;4. cooling device;5. self-checking device; 11. bromine measuring tank;12. main hand-operated valve;21. hand-operated valve;22. stop valve;23. metering pump;31. reaction kettle;32. blender;41. Chilled brine water inlet pipe;42. chilled brine return pipe;43. flowmeter;44. chilled brine return water water pump.
Specific embodiment
It is practical new below in conjunction with this to keep the objectives, technical solutions, and advantages of the embodiments of the present invention clearer Attached drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described.Obviously, it is retouched The embodiment stated is the utility model a part of the embodiment, instead of all the embodiments.Based on the implementation in the utility model Example, every other embodiment obtained by those of ordinary skill in the art without making creative efforts belong to The range of the utility model protection.
Embodiment one:
A kind of tetrabromobisphenol A synthesis procedure as shown in Figure 1 adds bromine device automatically, including bromine discharging device 1 and and its It is fed by the control metering device 2 that pipeline is connected into reaction unit 3, cooling device 4 is equipped with outside the reaction unit, also Including self-checking device 5;Wherein the bromine discharging device include bromine measuring tank 11 and with bromine measuring tank outlet master it is manual Valve 12;The control metering device includes hand-operated valve 21, stop valve 22 and metering pump 23, after the stop valve and metering series connection of pumps It is in parallel with hand-operated valve;The reaction unit includes reaction kettle 31 and the blender being set to inside reaction kettle 32;The cooling Device includes chilled brine water inlet pipe 41 and chilled brine return pipe 42, and the chilled brine return pipe is equipped with 43 He of flowmeter Chilled brine back water pump 44.
Wherein the self-checking device receives the weight from bromine measuring tank and feeds back, the switch feedback from stop valve, Velocity feedback and pressure leakage detection feedback from metering pump, the frequency feedback from blender, the flow feedback from flowmeter, The temperature of operation feedback and chilled brine water inlet pipe, chilled brine return pipe and reaction kettle from chilled brine back water pump is anti- Feedback.
Wherein the self-checking device sends switch command to stop valve to metering pump transmission speed adjustment signal, right Chilled brine sends start stop command, sends blowing to the external world and reminds.
Further wherein, the chilled brine back water pump can be by long-range and on the spot control.
Although the embodiments of the present invention have been shown and described above, it is to be understood that above-described embodiment is Illustratively, it should not be understood as limiting the present invention, those skilled in the art are in the original for not departing from this creation It can make changes, modifications, alterations, and variations to the above described embodiments within the scope of the invention in the case where reason and objective, to it Simple combination variation is carried out all to be classified as within the protection of the utility model.

Claims (4)

1. a kind of tetrabromobisphenol A synthesis procedure adds bromine device automatically, it is characterised in that: including bromine discharging device (1) and and its The control metering device (2) being connected by pipeline charging into reaction unit (3), the reaction unit outside are equipped with cooling device It (4), further include self-checking device (5);Wherein the bromine discharging device includes bromine measuring tank (11) and goes out with bromine measuring tank The main hand-operated valve (12) of mouth;The control metering device includes hand-operated valve (21), stop valve (22) and metering pump (23), described to cut Disconnected valve is in parallel with hand-operated valve with after metering series connection of pumps;The reaction unit includes reaction kettle (31) and is set to inside reaction kettle Blender (32);The cooling device includes chilled brine water inlet pipe (41) and chilled brine return pipe (42), the freezing Salt water return pipe is equipped with flowmeter (43) and chilled brine back water pump (44).
2. a kind of tetrabromobisphenol A synthesis procedure according to claim 1 adds bromine device automatically, it is characterised in that: it is described from Dynamic regulating device receives the weight from bromine measuring tank and feeds back, the switch feedback from stop valve, and the speed from metering pump is anti- Feedback and pressure leakage detection feedback, the frequency feedback from blender, the flow feedback from flowmeter come from chilled brine back water pump Operation feedback and chilled brine water inlet pipe, chilled brine return pipe and reaction kettle temperature feedback.
3. a kind of tetrabromobisphenol A synthesis procedure according to claim 1 adds bromine device automatically, it is characterised in that: it is described from Dynamic regulating device sends switch command to metering pump transmission speed adjustment signal, to stop valve, sends start and stop life to chilled brine It enables, blowing is sent to the external world and is reminded.
4. a kind of tetrabromobisphenol A synthesis procedure according to claim 1 adds bromine device automatically, it is characterised in that: described cold Freezing salt water back water pump can be by remotely and/or on the spot controlling.
CN201820885833.4U 2018-06-08 2018-06-08 A kind of tetrabromobisphenol A synthesis procedure adds bromine device automatically Active CN208711665U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820885833.4U CN208711665U (en) 2018-06-08 2018-06-08 A kind of tetrabromobisphenol A synthesis procedure adds bromine device automatically

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820885833.4U CN208711665U (en) 2018-06-08 2018-06-08 A kind of tetrabromobisphenol A synthesis procedure adds bromine device automatically

Publications (1)

Publication Number Publication Date
CN208711665U true CN208711665U (en) 2019-04-09

Family

ID=65971313

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820885833.4U Active CN208711665U (en) 2018-06-08 2018-06-08 A kind of tetrabromobisphenol A synthesis procedure adds bromine device automatically

Country Status (1)

Country Link
CN (1) CN208711665U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108786662A (en) * 2018-06-08 2018-11-13 山东金宜善新材料有限公司 A kind of tetrabromobisphenol A synthesis procedure adds bromine device and its control method automatically

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108786662A (en) * 2018-06-08 2018-11-13 山东金宜善新材料有限公司 A kind of tetrabromobisphenol A synthesis procedure adds bromine device and its control method automatically

Similar Documents

Publication Publication Date Title
CN108786662A (en) A kind of tetrabromobisphenol A synthesis procedure adds bromine device and its control method automatically
CN208711665U (en) A kind of tetrabromobisphenol A synthesis procedure adds bromine device automatically
CN106010649A (en) Chlorinated paraffin continuous production process efficiently utilizing chlorine gas
CN205340651U (en) A cooling agitated vessel for fire retardant production
CN114277393A (en) Electrolytic hydrogen production heat energy recycling system and control method thereof
CN204429286U (en) A kind of Temperature-controlled appliance of reactor
CN103676894A (en) Safety interlocking control system of trichloroethylene chlorination synthesizing device
CN216998608U (en) Electrolytic hydrogen production heat energy cyclic utilization system
CN106882767B (en) A kind of novel chloride and strong sulfuric acid response for hydrogen chloride preparation from rate controlling with from stirred reactor and method
CN203404988U (en) Water heater system
CN106748746A (en) A kind of isooctyl acid production system
CN107673311A (en) A kind of continuous device and method for preparing the high-concentrated sodium hypochlorite aqueous solution
CN207619019U (en) A kind of continuous device for preparing high-concentrated sodium hypochlorite aqueous solution
CN201785327U (en) System for preparing epoxypropane by chlorhydrin method
CN207520993U (en) A kind of aeration reaction kettle
CN211936523U (en) Copper sulfate stirring and dissolving device
CN204490837U (en) Mortar online recycling equipment
CN205253063U (en) Reation kettle heats closed loop control system
CN205121365U (en) Brown granulated sugar goes back to constant current system of dissolving
CN204644190U (en) A kind of heat circulation production line of concrete admixture
CN109464941A (en) A kind of full-automatic adder-subtractor and add alkali method
CN204816530U (en) CSTR temperature compensating control system
CN214376059U (en) Safe water circulation type temperature control machine
CN211159793U (en) Novel chlorination reaction kettle
CN204544174U (en) A kind of dropwise reaction blast protection system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant