CN201864681U - One-step solid epoxy resin water-saving production system - Google Patents

One-step solid epoxy resin water-saving production system Download PDF

Info

Publication number
CN201864681U
CN201864681U CN2010206145942U CN201020614594U CN201864681U CN 201864681 U CN201864681 U CN 201864681U CN 2010206145942 U CN2010206145942 U CN 2010206145942U CN 201020614594 U CN201020614594 U CN 201020614594U CN 201864681 U CN201864681 U CN 201864681U
Authority
CN
China
Prior art keywords
water
washing
reactor
wastewater
water tank
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 - Lifetime
Application number
CN2010206145942U
Other languages
Chinese (zh)
Inventor
朱新宝
周孜
程振溯
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.)
Anhui Hengyuan Chemical Co Ltd
Anhui Xinyuan Chemical Co ltd
LIANYUNGANG ZHIYUAN CHEMICAL CO Ltd
Original Assignee
LIANYUNGANG ZHIYUAN CHEMICAL CO Ltd
ANHUI HENGYUAN CHEMICAL 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 LIANYUNGANG ZHIYUAN CHEMICAL CO Ltd, ANHUI HENGYUAN CHEMICAL Co Ltd filed Critical LIANYUNGANG ZHIYUAN CHEMICAL CO Ltd
Priority to CN2010206145942U priority Critical patent/CN201864681U/en
Application granted granted Critical
Publication of CN201864681U publication Critical patent/CN201864681U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Treatment Of Water By Ion Exchange (AREA)

Abstract

The utility model relates to a production system adopting a one-step process to produce solid epoxy resin, which comprises a reaction kettle, and a suction device used for sucking material washing wastewater in the kettle, wherein a water outlet of the suction device is provided with a bypass pipe, the bypass pipe is led into a water storage tank, and liquid in the water storage tank is conveyed into the reaction kettle by a water pipe. So washing wastewater in the reaction kettle for washing products in previous times is still discharged from the water outlet of the suction device, the washing wastewater for washing in last times can be conveyed to the water storage tank for storage and then is sent into the reaction kettle by a pipeline to be used as washing raw water for the washing in previous times of next kettle reaction, and because the concentration of residual sodium chloride in the washing wastewater for washing in last times is low, the wastewater can be used as the washing raw water for washing in previous times of epoxy resin coarse products containing high-concentration sodium chloride, and the washing effect is not affected, but water consumption in the epoxy resin washing process is greatly saved so as to save water sources and reduce the production cost, the amount of wastewater treatment and treatment cost.

Description

Single stage method solid epoxy water saving production system
Technical field
The utility model relates to the production system that adopts one-step technology to produce solid epoxy.
Background technology
The single stage method solid epoxy production of prior art is carried out in reactor usually, adds water washing after reacting completely and reacts thick product, to remove residual reaction raw materials and by product sodium-chlor etc.Be exactly directly to add the deionized water wash product in reactor usually in the production, washes is through suction unit sucking-off discharging then, in Resins, epoxy chloride ion content up to standard till.The water consumption of washing process is big like this, water cost height, and wastewater treatment capacity is big simultaneously, and cost for wastewater treatment is also very high.
Summary of the invention
The purpose of this utility model just provides a kind of water-saving solid epoxy single stage method production system.
The scheme that adopts is exactly: a kind of single stage method solid epoxy water saving production system, comprise reactor, be used for the suction unit of material washes in the sucking-off still, it is characterized in that: the water outlet of described suction unit is provided with bypass pipe, bypass pipe is passed into water tank, and the water in the water tank is transported in the reactor by water pipe.
When utilizing the production system production solid epoxy of technique scheme, be used for washing in the reactor, the processing of can classifying of the washes of purified product, several times washes still utilizes the water outlet discharging of suction unit just, after several times the washes of washing can be transported to water tank and store, washing former water several times as next still product of washing preceding then in pipeline is sent into reactor uses, because after several times the washing the washes temperature reach more than 80 ℃, sodium chloride concentration is very low, so what can be used as the thick product of Resins, epoxy that contains higher concentration sodium-chlor precedingly washs former water several times and uses, this is to not influence of washing effect, but so but saved the water consumption of washing procedure greatly, water resources and heating steam consumption have been saved, reduce production cost, also alleviated the total amount and the processing cost of wastewater treatment.
Description of drawings
Fig. 1 is a synoptic diagram of the present utility model;
Fig. 2 is the synoptic diagram of the another kind of embodiment of the utility model.
Embodiment
A kind of single stage method solid epoxy water saving production system as shown in Figure 1, comprise reactor 1 and suction unit 2, suction unit 2 is used for the washes behind the product in the sucking-off washing still, the water outlet of suction unit 2 is provided with bypass pipe, bypass pipe is passed into water tank 3, and the water body in the water tank 3 can be transported in the reactor 1 by water pipe.That is to say that the water outlet at original suction unit 2 has increased bypass pipe, such washes that pumps out can discharge as originally, also can send into water tank 3 through bypass pipe and store stand-by.
Can have multiplely as for the mode that the water bodys in the water tank 3 is transported to reactor 1, modally be exactly: the fluid pump 6 that on the water outlet of water tank 3 and reactor 1 pipeline between directly, is provided for carrying washes.Because with the washes sucking-off, so need not to be provided with fluid pump 6 equipment such as grade on this section pipeline, 6 of fluid pumps mainly are that the materials in the water tank 3 will be sent back in the reactor 1 again as the former water use of washing to suction unit 2 itself again by vacuum tightness.The fluid conveying is quick and convenient like this, and the installation site of equipment is not strict with yet.
Perhaps as shown in Figure 2, the water outlet position of suction unit 2 is higher than the water inlet position of water tank 3, and the water outlet position of water tank 3 is higher than the position of reactor 1 and is communicated with by pipeline with reactor 1 top.Just the installation site of suction unit 2 is the highest, water tank 3 takes second place, reactor 1 is minimum, and washes is discharged the back by suction unit 2 water outlets and flowed into water tank 3 naturally like this, is put in the reactor 1 when needing then again.So just need not fluid pump 6 is set, be beneficial to energy-conservation.
Certainly, it is common practise that valve pilot piping break-make is set on each equipment and the pipeline, need not superfluous words.
Further, best described water tank is provided with a plurality of and is connected with the water outlet of suction unit 2 with bypass pipe respectively.Be provided with two exactly as Fig. 2, the washes after so each washing can be stored in respectively in the different water tank 3,4.So just can utilize respectively, be convenient to control and the concentration difference when improving the recycling washes and washing, improve overall detersive efficiency containing the residue washes different with byproduct concentration.By experience, described water tank preferably is provided with two; Can be convenient to reclaim washes, simultaneously also unreasonable operating device cost.The water outlet of water tank 3,4 is communicated to test tank 5, and the outlet position of test tank 5 is higher than reactor 1 position and is communicated with by pipeline with reactor 1 upper end.That is to say that water tank 3,4 just is provided with two, be respectively applied for the washes of collecting the 1st, 2 time reciprocal and get final product that previous washes can directly be discharged into the sewage disposal operation because concentration is higher.The setting of test tank 5 is for the accurate water consumption of control washing, avoids adding water excess or deficiency, has not only guaranteed washing effect simultaneously but also water saving, also avoids the amount of the former water of washing in personnel's visual inspection still, is convenient to production operation, has also improved processing safety.
Now introduce its preferred usage of native system in conjunction with the accompanying drawings in detail.At first reaction mass is added in the reactor 1 by proportioning and react, the after scouring reactor product is finished in reaction, washs altogether 7 times.Be exactly specifically: the 6th time the washes that the former water conservancy of the 1st washing was produced with the last time in the water tank 3; After finishing, the 1st washing utilize the discharging of suction unit 2 sucking-off washess; The 2nd detergent the 7th washes cleaning product of production last time that stores in the water tank 4, the washing influent density that adds in the reactor 1 reduces gradually like this, the residue of material also reduces gradually in the still, and the concentration difference of washing former water and material is totally maximum, and washing effect is still fine.The the 3rd to 7 time the former water of washing directly all can with tap water or steam condensate then.3rd, the washes of 4,5 washings send Waste Water Treatment because concentration is higher after directly utilizing suction unit 2 sucking-offs, cooling, recovery aged resin; The washes of the 6th washing is sent into the 1st time of producing as next time in the water tank 3 and is washed former water and use, and the washes of the 7th washing is sent into the 2nd time of producing as next time in the water tank 4 and washed former water and use.Product after washing finishes dewaters, filters processing treatment such as discharging, cooling, pulverizing.Utilize such system's washing effect can change hardly; And water consumption can save 2/7ths, just about 30 percent.Not only save water consumption greatly, saved water resources, reduced production cost, also alleviated the total amount and the processing cost of wastewater treatment.And serialization produce in because the surplus temperature of washes is still higher, so also shortened the heat-up time in still when washing former water, reduced the heating steam consumption, the effect that further reaches energy-saving and emission-reduction and enhance productivity.
Obviously such production system also is fit to produce other product and utilizes in the production that other liquid washs, and reaches energy saving purposes.

Claims (5)

1. single stage method solid epoxy water saving production system, comprise reactor (1), be used for the suction unit (2) of material washes in the sucking-off still, it is characterized in that: the water outlet of described suction unit (2) is provided with bypass pipe, bypass pipe is passed into water tank, and the liquid in the water tank can be transported in the reactor (1) by water pipe.
2. single stage method solid epoxy water saving production system according to claim 1, it is characterized in that: the water outlet position of described suction unit (2) is higher than the water inlet position of water tank, and the water outlet position of water tank is higher than the position of reactor (1) and is communicated with by pipeline with reactor (1) top.
3. single stage method solid epoxy water saving production system according to claim 1, it is characterized in that: the water outlet of described water tank is provided for carrying the fluid pump (6) of washes.
4. according to claim 2 or 3 described single stage method solid epoxy water saving production systems, it is characterized in that: described water tank is provided with a plurality of and uses bypass pipe to be connected with the water outlet of suction unit (2) respectively.
5. single stage method solid epoxy water saving production system according to claim 4, it is characterized in that: described water tank is provided with two; The water outlet of water tank (3,4) is communicated to test tank (5), and the outlet position of test tank (5) is higher than reactor (1) position and is communicated with by pipeline with reactor (1) upper end.
CN2010206145942U 2010-11-18 2010-11-18 One-step solid epoxy resin water-saving production system Expired - Lifetime CN201864681U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010206145942U CN201864681U (en) 2010-11-18 2010-11-18 One-step solid epoxy resin water-saving production system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010206145942U CN201864681U (en) 2010-11-18 2010-11-18 One-step solid epoxy resin water-saving production system

Publications (1)

Publication Number Publication Date
CN201864681U true CN201864681U (en) 2011-06-15

Family

ID=44135843

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010206145942U Expired - Lifetime CN201864681U (en) 2010-11-18 2010-11-18 One-step solid epoxy resin water-saving production system

Country Status (1)

Country Link
CN (1) CN201864681U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113817137A (en) * 2020-06-18 2021-12-21 南通星辰合成材料有限公司 Method for recycling epoxy chloropropane wastewater and method for preparing epoxy resin

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113817137A (en) * 2020-06-18 2021-12-21 南通星辰合成材料有限公司 Method for recycling epoxy chloropropane wastewater and method for preparing epoxy resin
CN113817137B (en) * 2020-06-18 2023-10-10 南通星辰合成材料有限公司 Recycling method of epichlorohydrin wastewater and preparation method of epoxy resin

Similar Documents

Publication Publication Date Title
CN103922500B (en) Zero discharge processor for electronickelling rinsing waste water and processing method thereof
CN202376824U (en) Device for recycling white carbon black filter cake washed water
CN109735968A (en) A kind of spent lye recoverying and utilizing method
CN201864681U (en) One-step solid epoxy resin water-saving production system
CN201305523Y (en) Processing system for transforming normal water to ultrapure water
CN204661332U (en) A kind of recovery system of potassium catalyzer
CN115625181A (en) Phosphogypsum harmless treatment system
CN201634548U (en) Treatment system for reclaiming grinding waste water into ultrapure water in semiconductor industry
CN201882932U (en) Device for reusing cleaning waste water of silicon chips
CN115557719A (en) Comprehensive treatment method of phosphogypsum
CN201420167Y (en) Recycling system of lye
CN204162410U (en) The harmless treatment unit of waste silicon powder
CN201596467U (en) Concentrated water reuse system for reverse osmosis unit
CN102153223A (en) Sodium carboxymethylcellulose industrial sewage recycling device
CN207567018U (en) A kind of photovoltaic silicon wafer production wastewater treatment device
CN201990574U (en) Beer production waste water treatment system
CN102416297A (en) Technical method for recovering waste alkali liquor with composite ceramic membrane in washing of beer bottles
CN201999825U (en) Sodium carboxy methyl cellulose industrial sewage recycling device
CN204454591U (en) A kind of device utilizing high temperature slurry filtration gas heat energy
CN202808460U (en) Flocculant production equipment and device for separating and cleaning fly ash feed liquid
CN202016926U (en) Sodium carboxymethylcellulose industrial sewage treatment device
CN102153225B (en) Sodium carboxymethylcellulose industrial sewage treatment device
CN204162543U (en) Nanofiltration strengthens concentrated strong brine device in conjunction with chelate separation process
CN204125192U (en) The useless time sodium recycle device of acetylene
CN203079892U (en) Recycling device of washing water in polyvinyl butyral synthesis industry

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 245900 No. 16 Zijin Road, Circular Economy Park, Huizhou District, Anhui, Huangshan City

Co-patentee after: LIANYUNGANG ZHIYUAN CHEMICAL Co.,Ltd.

Patentee after: ANHUI HENGYUAN CHEMICAL CO.,LTD.

Address before: 245900 No. 21-9 East Huizhou Road, Huizhou District, Anhui, Huangshan City

Co-patentee before: Lianyungang Zhiyuan Chemical Co.,Ltd.

Patentee before: ANHUI HENGYUAN CHEMICAL Co.,Ltd.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20191205

Address after: 245900 No. 16 Zijin Road, Circular Economy Park, Huizhou District, Anhui, Huangshan City

Patentee after: ANHUI XINYUAN CHEMICAL Co.,Ltd.

Address before: 245900 No. 16 Zijin Road, Circular Economy Park, Huizhou District, Anhui, Huangshan City

Co-patentee before: Lianyungang Zhiyuan Chemical Co.,Ltd.

Patentee before: ANHUI HENGYUAN CHEMICAL CO.,LTD.

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20110615