CN106430381A - Pueraria starch processing wastewater concentrating unit - Google Patents
Pueraria starch processing wastewater concentrating unit Download PDFInfo
- Publication number
- CN106430381A CN106430381A CN201611140156.5A CN201611140156A CN106430381A CN 106430381 A CN106430381 A CN 106430381A CN 201611140156 A CN201611140156 A CN 201611140156A CN 106430381 A CN106430381 A CN 106430381A
- Authority
- CN
- China
- Prior art keywords
- concentration tank
- tank
- level
- primary
- starch processing
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D407/00—Heterocyclic compounds containing two or more hetero rings, at least one ring having oxygen atoms as the only ring hetero atoms, not provided for by group C07D405/00
- C07D407/02—Heterocyclic compounds containing two or more hetero rings, at least one ring having oxygen atoms as the only ring hetero atoms, not provided for by group C07D405/00 containing two hetero rings
- C07D407/04—Heterocyclic compounds containing two or more hetero rings, at least one ring having oxygen atoms as the only ring hetero atoms, not provided for by group C07D405/00 containing two hetero rings directly linked by a ring-member-to-ring-member bond
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/02—Temperature
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/44—Time
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The invention provides a pueraria starch processing wastewater concentrating unit. The pueraria starch processing wastewater concentrating unit comprises a steam generating furnace, a wastewater collection pool, a concentration tank device, an electric heater and a finished product collecting pool, wherein the concentration tank device is a three-stage concentration tank device, a primary concentration tank therein adopts steam heating, and a secondary concentration tank and a tertiary concentration tank therein adopt compound heating of steam heating and electrical heating. The pueraria starch processing wastewater concentrating unit has the advantages that the three-stage concentration tank device is employed, concentration temperatures of the primary concentration tank, the secondary concentration tank and the tertiary concentration tank are increased sequentially, pueraria starch processing wastewater is concentrated into puerarin pulp liquid containing 30-40% of water once, and subsequent drying and grinding of the puerarin slurry are facilitated so as to obtain puerarin; the pueraria starch processing wastewater concentrating unit is short in concentration time and high in production efficiency.
Description
Technical field
The present invention relates to the Waste water concentrating machine after the waste water reprocessing after Radix Puerariae starch processing, especially Radix Puerariae starch processing
Group.
Background technology
At present, Radix Puerariae starch manufacturing enterprise, then many with Radix Puerariae as raw material, Radix Puerariae starch is obtained by following procedure of processing,
Procedure of processing is：1. the Radix Puerariae that cleaning is gathered；2. Radix Puerariae is crushed, obtain Radix Puerariae serosity；3. the centrifugation of Radix Puerariae serosity goes out fiber, obtains
Amyloid separation serosity；4. serosity being separated by dehydration, drying, obtains Radix Puerariae starch, and the waste water after being dehydrated directly is arranged
Put.
The problem of presence is：The production technology of Radix Puerariae starch has then only been focused on obtaining this single product of starch, and discharges
Waste water in contain puerarin, cause the significant wastage of resource.
Content of the invention
For the waste water reuse after extracting to Radix Puerariae starch, the present invention proposes the Waste water concentrating machine after Radix Puerariae starch processing
Group, the device structure is simple, Waste water concentrating can be become puerarin serosity.
For achieving the goal, the present invention is adopted the following technical scheme that：Waste water concentrating unit after Radix Puerariae starch processing, including steaming
Vapour producer, wastewater collection pond, concentration tank arrangement, electric heater, finished product collecting pit,
It is characterized in that：It is that three-level concentrates tank arrangement to concentrate tank arrangement, concentrates including primary concentration tank, secondary concentration tank, three-level
Tank, the outlet of primary concentration tank is connected with the import of secondary concentration tank by the first suction pump, pipeline, the going out of secondary concentration tank
Mouth is connected with the import of three-level concentration tank by the second suction pump, pipeline；
The import of the primary concentration tank is connected with wastewater collection pond by water pump, pipeline, and the outlet of the three-level concentration tank is led to
Cross the 3rd suction pump, pipeline and be connected to finished product collecting pit；
The steam (vapor) outlet of Steam generating furnace is connected with the discharge for concentrating above tank arrangement by valve, and discharge connection is led to respectively
Cross gas collection to be in charge of to primary concentration tank, secondary concentration tank, three-level concentration tank inner chamber；
Described electric heater is two, and two electric heaters are separately mounted to secondary concentration tank, the bottom of three-level concentration tank；
Thermometer, air vent are respectively equipped with the primary concentration tank, secondary concentration tank, three-level concentration tank.
Restriction further to technique scheme：The concentration parameter of primary concentration tank is：45-50 DEG C of thickening temperature, when
Between 50-60min；The concentration parameter of secondary concentration tank is：60-65 DEG C of thickening temperature, time 65-75min；Three-level concentration tank dense
Contracting parameter is：70-75 DEG C of thickening temperature, time 50-60min.
Beneficial effect：The present invention using three-level concentrate tank arrangement, and successively improve primary concentration tank, secondary concentration tank,
The thickening temperature of three-level concentration tank（45-50）Waste water concentrating after disposably Radix Puerariae starch being processed to water content be 30-
40% puerarin serosity, subsequently drying, crushing obtain puerarin to be easy to puerarin serosity；The present invention is multiple using steam, electrical heating
Close heating to concentrate, and improve primary concentration tank, secondary concentration tank, the thickening temperature of three-level concentration tank successively, concentration time is short,
Production efficiency height.
Description of the drawings
Fig. 1 is the structural representation of the present invention.
Specific embodiment
In conjunction with shown in Fig. 1, the present invention is further described as follows：Waste water concentrating unit after Radix Puerariae starch processing, including useless
Water collecting pit 1, Steam generating furnace 2, concentration tank arrangement, electric heater 15, finished product collecting pit 13, it is that three-level is concentrated to concentrate tank arrangement
Tank arrangement, including primary concentration tank 6, secondary concentration tank 8, three-level concentration tank 12, the outlet of primary concentration tank 6 is aspirated by first
Pump 17, pipeline is connected with the import of secondary concentration tank 8, the outlet of secondary concentration tank 8 passes through the second suction pump 16, pipeline and three
The import connection of level concentration tank 12；
The import of the primary concentration tank 6 is connected with wastewater collection pond 1 by water pump 18, pipeline, the three-level concentration tank 12
Outlet is connected to finished product collecting pit 13 by the 3rd suction pump 14, pipeline；
The steam (vapor) outlet of Steam generating furnace 2 is connected 4 by valve 3 with the discharge for concentrating above tank arrangement, discharge connection point
It is not in charge of by gas collection（Label 5,7,9）To primary concentration tank, secondary concentration tank, three-level concentration tank inner chamber；
Described electric heater 15 is two, and two electric heaters 15 are separately mounted to secondary concentration tank 8, three-level concentration tank 12
Bottom；
Thermometer 10, air vent 11 is respectively equipped with the primary concentration tank 6, secondary concentration tank 8, three-level concentration tank 12.
Restriction further to Waste water concentrating unit：The concentration parameter of primary concentration tank is：45-50 DEG C of thickening temperature, when
Between 50-60min；The concentration parameter of secondary concentration tank is：60-65 DEG C of thickening temperature, time 65-75min；Three-level concentration tank dense
Contracting parameter is：70-75 DEG C of thickening temperature, time 50-60min.
Waste water concentrating after the present invention disposably can process Radix Puerariae starch is starched to the puerarin that water content is 30-40%
Liquid, obtains puerarin block by follow-up lyophilization, crushing.
Claims (2)
1. the Waste water concentrating unit after Radix Puerariae starch processing, including Steam generating furnace, wastewater collection pond, concentrates tank arrangement, and electricity adds
Hot device, finished product collecting pit,
It is characterized in that：It is that three-level concentrates tank arrangement to concentrate tank arrangement, concentrates including primary concentration tank, secondary concentration tank, three-level
Tank, the outlet of primary concentration tank is connected with the import of secondary concentration tank by the first suction pump, pipeline, the going out of secondary concentration tank
Mouth is connected with the import of three-level concentration tank by the second suction pump, pipeline；
The import of the primary concentration tank is connected with wastewater collection pond by water pump, pipeline, and the outlet of the three-level concentration tank is led to
Cross the 3rd suction pump, pipeline and be connected to finished product collecting pit；
The steam (vapor) outlet of Steam generating furnace is connected with the discharge for concentrating above tank arrangement by valve, and discharge connection is led to respectively
Cross gas collection to be in charge of to primary concentration tank, secondary concentration tank, three-level concentration tank inner chamber；
Described electric heater is two, and two electric heaters are separately mounted to secondary concentration tank, the bottom of three-level concentration tank；
Thermometer, air vent are respectively equipped with the primary concentration tank, secondary concentration tank, three-level concentration tank.
2. the Waste water concentrating unit after Radix Puerariae starch according to claim 1 is processed, it is characterised in that：Primary concentration tank
Concentrating parameter is：45-50 DEG C of thickening temperature, time 50-60min；The concentration parameter of secondary concentration tank is：Thickening temperature 60-65
DEG C, time 65-75min；The concentration parameter of three-level concentration tank is：70-75 DEG C of thickening temperature, time 50-60min.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611140156.5A CN106430381A (en) | 2016-12-12 | 2016-12-12 | Pueraria starch processing wastewater concentrating unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611140156.5A CN106430381A (en) | 2016-12-12 | 2016-12-12 | Pueraria starch processing wastewater concentrating unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106430381A true CN106430381A (en) | 2017-02-22 |
Family
ID=58216872
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611140156.5A Withdrawn CN106430381A (en) | 2016-12-12 | 2016-12-12 | Pueraria starch processing wastewater concentrating unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106430381A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109260780A (en) * | 2018-12-04 | 2019-01-25 | 重庆凡勇食品有限公司 | A kind of Starch Production process equipment |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5503810A (en) * | 1993-06-04 | 1996-04-02 | Chang; William | System for producing herbal concentrate |
| CN100998782A (en) * | 2006-01-12 | 2007-07-18 | 广州王老吉药业股份有限公司 | Traditional Chinese medicine oral liquid for treating gastrointestinal disease and its preparing method |
| WO2010034134A1 (en) * | 2008-09-25 | 2010-04-01 | Weng Xiaotao | Preparation method of concentrated pill of chinese medicine |
| CN201733819U (en) * | 2010-07-14 | 2011-02-09 | 紫山丸善(龙海)果菜加工有限公司 | Main structure of thickener |
| CN103478643A (en) * | 2013-09-25 | 2014-01-01 | 湖北省宏源药业有限公司 | Comprehensive utilization method for waste water and fibroid dregs generated from arrowroot production |
-
2016
- 2016-12-12 CN CN201611140156.5A patent/CN106430381A/en not_active Withdrawn
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5503810A (en) * | 1993-06-04 | 1996-04-02 | Chang; William | System for producing herbal concentrate |
| CN100998782A (en) * | 2006-01-12 | 2007-07-18 | 广州王老吉药业股份有限公司 | Traditional Chinese medicine oral liquid for treating gastrointestinal disease and its preparing method |
| WO2010034134A1 (en) * | 2008-09-25 | 2010-04-01 | Weng Xiaotao | Preparation method of concentrated pill of chinese medicine |
| CN201733819U (en) * | 2010-07-14 | 2011-02-09 | 紫山丸善(龙海)果菜加工有限公司 | Main structure of thickener |
| CN103478643A (en) * | 2013-09-25 | 2014-01-01 | 湖北省宏源药业有限公司 | Comprehensive utilization method for waste water and fibroid dregs generated from arrowroot production |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109260780A (en) * | 2018-12-04 | 2019-01-25 | 重庆凡勇食品有限公司 | A kind of Starch Production process equipment |
| CN109260780B (en) * | 2018-12-04 | 2024-01-26 | 重庆凡勇食品有限公司 | Starch production and processing equipment |
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Application publication date: 20170222 |
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