CN205821285U - Containing in soap and profit scouring water reclaiming system - Google Patents

Containing in soap and profit scouring water reclaiming system Download PDF

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Publication number
CN205821285U
CN205821285U CN201620735142.7U CN201620735142U CN205821285U CN 205821285 U CN205821285 U CN 205821285U CN 201620735142 U CN201620735142 U CN 201620735142U CN 205821285 U CN205821285 U CN 205821285U
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CN
China
Prior art keywords
water
soap
connects
centrifuge
acid
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
Application number
CN201620735142.7U
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Chinese (zh)
Inventor
邹强
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.)
Guangzhou Keruibo Electromechanical Technology Co Ltd
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Guangzhou Keruibo Electromechanical Technology Co Ltd
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Priority to CN201620735142.7U priority Critical patent/CN205821285U/en
Application granted granted Critical
Publication of CN205821285U publication Critical patent/CN205821285U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/74Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes

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Abstract

nullThis utility model provides and contains in soap and profit scouring water reclaiming system,Including de-soap system and Water circulation system,Described de-soap system includes hot-water cylinder、Heat-exchanger pump、Divide water bag、De-soap centrifuge、Blender、Washing centrifuge,Described hot-water cylinder is provided with water inlet、Overflow pipe,Described point of water bag is provided with overfall,Water bag is divided to be also connected with blender and washing centrifuge,De-soap centrifuge connects Fructus Gleditsia tank,Described blender connects acid starting material tank,Described acid starting material tank is provided with isocon,Described Water circulation system includes steam heater、Water acid adding mixed organization,Its front end of described steam heater connects described overflow pipe、Overfall,Its end of steam heater has ratio adjusting valve,Described ratio adjusting valve connects de-soap centrifuge and washing centrifuge,Described its front end of water acid adding mixed organization connects isocon,Water its end of acid adding mixed organization connects blender.This utility model, can effectively save water consumption and energy resource consumption owing to being provided with Water circulation system.

Description

Containing in soap and profit scouring water reclaiming system
Technical field
This utility model relates to refining raw food oil apparatus field, in particular to containing in soap and profit scouring water reuse System.
Background technology
In edible oil and fat refine and workshop section, need the neutralization oil containing soap is washed so that it is near containing soap Below 100ppm, the technique that each factory uses now is: hair hot heat exchange acid is added mixing and added with reaction base Add mixing to take off soap with reaction homoiothermic centrifugation to mix (hot water+citric acid or phosphoric acid) homoiothermic centrifugation de- Water is dried, flushing water washing water, sealing water flushing water, sealing water and centrifugal point produced in wherein centrifugal dewatering step The separation water produced in dehydration will enter diversion box, and the water after diversion box processes will be directly discharged to sewage disposal factory and office Reason.This technique not only waste water resource, it is impossible to give full play to the effect of washing water, and it is normal to need to expend substantial amounts of energy warms The fresh water of temperature, furthermore during sewage disposal, difficulty and cost are the biggest.Therefore, design one can be with effective recycling containing in soap With the equipment of the washing water after use in oil technique, there is bigger effect.
Utility model content
It is directly sent to sewage disposal device containing in soap and after the washing water of use uses in oil washing process, wave for general Take resource and relatively costly problem, it is provided that containing in soap and profit scouring water reclaiming system.
Containing in soap and profit scouring water reclaiming system, including de-soap system and Water circulation system, described de-soap system includes Hot-water cylinder, heat-exchanger pump, Fen Shuibao, de-soap centrifuge, blender, washing centrifuge, above-mentioned parts connect according to sequencing, described Hot-water cylinder is provided with water inlet, overflow pipe, and described point of water bag is provided with overfall, and it is centrifugal with washing that Fen Shuibao is also connected with blender Machine, de-soap centrifuge connects Fructus Gleditsia tank, and described blender connects has acid starting material tank, described acid starting material tank to be provided with isocon, Described Water circulation system includes steam heater, water acid adding mixed organization, and above-mentioned parts connect according to sequencing, and described soda pop is mixed Its front end of clutch connects described overflow pipe, overfall, and its end of steam heater has ratio adjusting valve, described ratio adjusting valve Connecting de-soap centrifuge and washing centrifuge, described its front end of water acid adding mixed organization connects isocon, water acid adding mixed organization Its end connects blender.
Further, described hot-water cylinder, Fructus Gleditsia tank and steam heater are respectively connected with steam pipeline.
Further, it is provided with water wash system connector before described water its entrance of acid adding mixed organization.
Further, described acid starting material tank citric acid or phosphoric acid have been deposited.
Further, described steam heater and water acid adding mixed organization are provided with discharge outlet.
The utility model has the advantage of, be provided with Water circulation system, set originally needing to be delivered directly to sewage disposal The standby water after washing processes and recycles, and is used by mixed liquor excessive for concentration new after a period of time has passed Fresh water cements out, and supplements because rinsing and the water of acid reaction consumption simultaneously, and circulation ratio can reach more than 85%, have Effect economizes on resources, and reduces production cost.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, the accompanying drawing in describing below is only It is embodiments more of the present utility model, for those of ordinary skill in the art, in the premise not paying creative work Under, it is also possible to other accompanying drawing is obtained according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
It is directly sent to sewage disposal device containing in soap and after the washing water of use uses in oil washing process, wave for general Take resource and relatively costly problem, it is provided that containing in soap and profit scouring water reclaiming system.
Make the purpose of this utility model embodiment, technical scheme and advantage clearer, below in conjunction with this utility model Accompanying drawing in embodiment, carries out clear, complete description to the technical scheme in this utility model embodiment, it is clear that described Embodiment be a part of embodiment of the present utility model rather than whole embodiments.Based on the enforcement in this utility model Example, the every other embodiment that those of ordinary skill in the art obtain under not making creative work premise, broadly fall into this The scope of utility model protection.
As it is shown in figure 1, contain in soap and profit scouring water reclaiming system, including de-soap system and Water circulation system, described de- Soap system includes hot-water cylinder 11, heat-exchanger pump 12, point water bag 13, de-soap centrifuge 14, blender 15, washing centrifuge 16, above-mentioned Parts connect according to sequencing, and described hot-water cylinder 11 is provided with water inlet 111, overflow pipe 112, and described point of water bag 13 is provided with excessive Head piece 131, a point water bag 13 is also connected with blender 15 and washing centrifuge 16, and de-soap centrifuge 14 connects Fructus Gleditsia tank 17, described Blender 15 connects acid starting material tank 18, has deposited citric acid or phosphoric acid in described acid starting material tank 18, and acid starting material tank 18 is provided with Isocon 181, described Water circulation system includes steam heater 21, water acid adding mixed organization 22, and above-mentioned parts are according to sequencing Connecting, described steam heater 21 is provided with discharge outlet 3, its entrance of water acid adding mixed organization 22 with water acid adding mixed organization 22 Before be provided with water wash system connector 221, its front end of steam heater 21 connects described overflow pipe 112, overfall 131, soda pop Its end of blender 21 has ratio adjusting valve 211, and described ratio adjusting valve 211 connects de-soap centrifuge 14 and washing centrifuge 16, described its front end of water acid adding mixed organization 22 connects isocon 181, and its end of water acid adding mixed organization 22 connects blender 15, described hot-water cylinder 11, Fructus Gleditsia tank 17 and steam heater 21 are respectively connected with steam pipeline 4.
Time actually used, containing in soap and oil enters de-soap centrifuge 14 by external pipe, containing in soap and oil is through de- After soap processes, Fructus Gleditsia composition enters into Fructus Gleditsia tank 17, neutralize oil component then enter in blender 15 with the acid in acid starting material tank 18 After mixed merga pass washing centrifuge 16 washing, output processes to next system.Carry out during this process equal in dewatering centrifuge 16 Needs are passed through and are entered hot-water cylinder 11 by water inlet 111, in hot-water cylinder 11 after steam heats and by heat-exchanger pump 12, point water bag 13 The hot water of distribution conveying.Hot water after using from washing centrifuge 16 enter into Water circulation system and with from hot-water cylinder 11, Fen Shui Wrapping the hot water that 13 overflows go out together to reheat through steam heater 21, then part hot water is laggard through ratio adjusting valve 211 Enter to wash and centrifuge 16 recycles and can lead to when needed de-soap centrifuge 14 be used as cleaning equipment, and another part is warm Water is sent back to after water acid adding mixed organization 22 supplemental acid content and is recycled at blender 15.In use due to concentration Rise, need from discharge outlet 3, be discharged to the outside old hot water sewage disposal device, and from hot-water cylinder 11, supplement new heat Water enters system.Owing to having water wash system connector 221, it is possible to use this interface is connected with original system, facilitates equipment Arrange.
The utility model has the advantage of, be provided with Water circulation system, set originally needing to be delivered directly to sewage disposal The standby water after washing processes and recycles, and is used by mixed liquor excessive for concentration new after a period of time has passed Fresh water cements out, and supplements because rinsing and the water of acid reaction consumption simultaneously, and circulation ratio can reach more than 85%, have Effect economizes on resources, and reduces production cost.
Above content is to combine concrete preferred implementation further detailed description of the utility model, it is impossible to Assert and of the present utility model be embodied as being confined to these explanations, the most all made impartial change and modification according to the application scope, All should still belong in this utility model covering scope.

Claims (5)

1. contain in soap and profit scouring water reclaiming system, including de-soap system and Water circulation system, it is characterised in that described de-soap System includes hot-water cylinder, heat-exchanger pump, Fen Shuibao, de-soap centrifuge, blender, washing centrifuge, and above-mentioned parts are according to sequencing Connecting, described hot-water cylinder is provided with water inlet, overflow pipe, and described point of water bag is provided with overfall, and Fen Shuibao is also connected with blender With washing centrifuge, de-soap centrifuge connects Fructus Gleditsia tank, and described blender connects acid starting material tank, and described acid starting material tank is arranged Having isocon, described Water circulation system to include steam heater, water acid adding mixed organization, above-mentioned parts connect according to sequencing, Its front end of described steam heater connects described overflow pipe, overfall, and its end of steam heater has ratio adjusting valve, described Ratio adjusting valve connects de-soap centrifuge and washing centrifuge, and described its front end of water acid adding mixed organization connects isocon, and water adds Acid its end of mixed organization connects blender.
Contain in soap the most according to claim 1 and profit scouring water reclaiming system, it is characterised in that described hot-water cylinder, Fructus Gleditsia Tank and steam heater are respectively connected with steam pipeline.
Contain in soap the most according to claim 1 and profit scouring water reclaiming system, it is characterised in that described water acid adding mixer It is provided with water wash system connector before its entrance of structure.
Contain in soap the most according to claim 1 and profit scouring water reclaiming system, it is characterised in that described acid starting material tank is deposited It is placed with citric acid or phosphoric acid.
The most according to claim 1 containing in soap and profit scouring water reclaiming system, it is characterised in that described steam heater with Water acid adding mixed organization is provided with discharge outlet.
CN201620735142.7U 2016-07-13 2016-07-13 Containing in soap and profit scouring water reclaiming system Expired - Fee Related CN205821285U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620735142.7U CN205821285U (en) 2016-07-13 2016-07-13 Containing in soap and profit scouring water reclaiming system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620735142.7U CN205821285U (en) 2016-07-13 2016-07-13 Containing in soap and profit scouring water reclaiming system

Publications (1)

Publication Number Publication Date
CN205821285U true CN205821285U (en) 2016-12-21

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114540117A (en) * 2022-02-28 2022-05-27 湖北新铭生物能源科技有限公司 Crude methyl ester soap removing equipment and method for recycling soap removing agent

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114540117A (en) * 2022-02-28 2022-05-27 湖北新铭生物能源科技有限公司 Crude methyl ester soap removing equipment and method for recycling soap removing agent
CN114540117B (en) * 2022-02-28 2023-08-18 湖北新铭生物能源科技有限公司 Crude methyl ester soap removal equipment and method for recycling soap removal agent

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CB03 Change of inventor or designer information

Inventor after: Qiu Qiang

Inventor before: Zou Qiang

CB03 Change of inventor or designer information
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20161221

Termination date: 20200713

CF01 Termination of patent right due to non-payment of annual fee