CN103520979A - Special vacuum-type drum filter for treating ultrafiltration tank bottom substances and treatment method of ultrafiltration tank bottom substances - Google Patents
Special vacuum-type drum filter for treating ultrafiltration tank bottom substances and treatment method of ultrafiltration tank bottom substances Download PDFInfo
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- CN103520979A CN103520979A CN201310481799.6A CN201310481799A CN103520979A CN 103520979 A CN103520979 A CN 103520979A CN 201310481799 A CN201310481799 A CN 201310481799A CN 103520979 A CN103520979 A CN 103520979A
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- enzymolysis liquid
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Abstract
The invention relates to a special vacuum-type drum filter for treating ultrafiltration tank bottom substances and a treatment method of ultrafiltration tank bottom substances. The special vacuum-type drum filter comprises a drum drive unit, a filter tank, a drum, a distributing head and a stirring device. The special vacuum-type drum filter is characterized in that one side wall of the inner bottom of the filter tank is provided with an ultrasonic generator; one side wall of the filter tank is provided with an enzymolysis solution inlet; and the enzymolysis solution inlet is connected with an enzymolysis solution input pump. The ultrafiltration tank bottom substance treatment machine provided by the invention can directly discharge the tank bottom substances to the tank bottom treatment procedure without on-line water dilution when the ultrafiltration reaches the cleaning period, shortens the cleaning time (1.5 hours of water dilution and liftout time for each cleaning period), greatly lowers the blockage and abrasion degree of the ultrafiltration membrane by activated carbon and other solid particle auxiliary materialss, and is beneficial to prolonging the service life of the ultrafiltration membrane.
Description
Technical field
The invention belongs to cleaning and drying device field, especially a kind of processing ultrafiltration tank bottoms Special vacuum rotary drum filter and ultrafiltration tank bottoms processing method.
Background technology
In fruit juice process, per production cycle of ultrafiltration operation finishes, in ultrafiltration circulating tank, save bit by bit the mixture of large carbon content active, fruit juice and other composition, be called tank bottoms, owing to wherein containing a large amount of fruit juice, hesitate to discard and increase cost of sewage disposal, processing mode is that the circulation that is diluted with water raising tank bottoms in ultrafiltration circulating tank runs well to guarantee ultrafiltration at present, thus as far as possible fruit juice of collecting wherein more.
This processing mode drawback is: be diluted with water the cleaning, the production time that have taken ultrafiltration; Add water and cause rear line evaporation capacity to strengthen, energy consumption increases; Juice extraction in tank bottoms is insufficient; Liquid tank bottoms is disposed to sewage plant has increased sewage disposal difficulty and cost.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art part, provide and process ultrafiltration tank bottoms Special vacuum rotary drum filter and ultrafiltration tank bottoms processing method, this vacuum-type drum filter has increased ultrasonic generator and enzymolysis liquid entrance on the basis of existing filter in lautertuns, open ultrasonic after, the separating rate that can increase fruit juice and active carbon improves tank bottoms disposal ability, increase the chocking-up degree that can reduce cloth soil after enzymolysis liquid, the fruit juice increasing after treatment effeciency reclaims can continue to use after the enzyme that goes out simultaneously.
The object of the invention is to be achieved through the following technical solutions:
A kind of processing ultrafiltration tank bottoms Special vacuum rotary drum filter, comprise rotary drum driving device, lautertuns, rotary drum, dispensing head, agitating device, it is characterized in that: inner bottom part one sidewall at lautertuns is installed a supersonic generator, at lautertuns one sidewall, be shaped with enzymolysis liquid entrance, enzymolysis liquid entrance connects enzymolysis liquid front pump.
And described enzymolysis liquid front pump adopts motor to drive.
Vacuum-type drum filter is processed a ultrafiltration tank bottoms processing method, and step is as follows:
(1) drum surface cloth is native: the rotary drum of vacuum-type drum filter is carried out to rotary drum and carry out cloth soil, cloth soil thickness 4cm, with native: perlite, thick soil, fine earth; Three kinds of soil is cycling coating in order repeatedly from inside to outside;
(2) after filling substrate being diluted with water, be placed in lautertuns, start agitating device, tank bottoms comprises the insoluble solids such as active carbon and fruit juice; Stir and open supersonic generator simultaneously, process 20-30 minute;
(3) pass into enzymolysis liquid, described enzymolysis liquid consists of: amylase, pectase, protease, cellulase, and its addition can regulate according to the content of insoluble solid in tank bottoms, and add and continue to stir 0.5-1 hour after enzymolysis liquid,
(4) led to after enzymolysis liquid and started drum drive unit, driven rotary drum to be rotated filtration, after filtering, active carbon is filtered to drum surface, when thickness to a certain extent after, with device for discharging, removed;
(5) the fruit juice that filters acquisition clings to and kills, and sterilization joins unified ultrafiltration and the subsequent step of carrying out in original fruit juice after the enzyme that goes out;
(6) the cloth of active carbon and drum surface soil one is logical removes as solid refuse.
And, tank bottoms disposal ability: 206kg/h.m after described cloth soil
2, fruit juice flux: 157.5kg/h.m after cloth soil
2.
And, during described cloth, after 2.5-3cm, be coated with fine earth, final coating layer thickness 4cm.
And, in described enzymolysis liquid, the addition of various enzymes is: amylase: diastatic addition is the 0.001-0.01% of tank bottoms weight, pectase: the addition of pectase is the 0.002-0.05% of tank bottoms weight, protease: the addition of protease is the 0.002-0.02% of tank bottoms weight; The addition of cellulase is the 0.002-0.05% of tank bottoms weight.
Advantage of the present invention and good effect are as follows:
1, ultrafiltration tank bottoms processor provided by the invention is fixedly mounted with Vltrasonic device in lautertuns, opens ultrasonicly when cleaning, and can be improved the separating rate of the impurity such as fruit juice and active carbon, insoluble solid, raising cleaning efficiency.
2, ultrafiltration tank bottoms processor provided by the invention is shaped with cleaning fluid at sidewall and adds entrance, can in main frame, add enzymolysis liquid, and the stickums such as the pectin in enzymolysis fruit juice, fiber, sugar improve cleaning efficiency.
3, ultrafiltration tank bottoms processor provided by the invention can directly be disposed to tank bottoms treatment process at the bottom of tank when ultrafiltration reaches the cleaning frequency, without being diluted with water online, shortened scavenging period simultaneously, per cleaning frequency is saved the liftout time that is diluted with water of 1.5h, simultaneously also significantly reduce the solid particle auxiliary materials such as active carbon to the obstruction of milipore filter and the degree of wear, be conducive to extend milipore filter service life.
4, this equipment is can be effectively separated and collect by other impurity such as the fruit juice in tank bottoms and active carbons.It is solid-state separated that the insoluble solids such as active carbon are, and can effectively reduce cost of sewage disposal.Tank bottoms crushing juice rate 76.54%.Leaching juice, to cross ultra-filtration flux relatively low.It is normal that tank bottoms leaches the concentrated rear indices of juice.
5, the solid-liquid separation effect of ultrafiltration tank bottoms processor provided by the invention is better, and fruit juice yield is higher, and the impurity such as the active carbon of separating, insoluble solid, with solid state garbage disposal, reduce cost of sewage disposal.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Fig. 2 vacuum-type drum filter operation flow chart.
The specific embodiment
Below in conjunction with embodiment, the present invention is further described, and following embodiment is illustrative, is not determinate, can not limit protection scope of the present invention with following embodiment.
A kind of processing ultrafiltration tank bottoms Special vacuum rotary drum filter, comprise rotary drum driving device 1, lautertuns 2, rotary drum 3, dispensing head 4, agitating device, rotary drum level is packed in lautertuns upper surface, rotary drum driving device is installed in rotary drum one end, rotary drum driving device drives rotary drum main shaft to rotate, the other end of rotary drum is installed dispensing head, on dispensing head, be shaped with three pipe connector lugs, connect respectively filtrate (liquid interface, compressed air inlet interface, vavuum pump interface, lautertuns inner bottom part is also installed agitating device (blocking in way, not shown).
Above-mentioned vacuum-type drum filter is except the device and structure of above narration, also comprise relevant connection pipeline etc., there is no detailed description, because the vacuum-type drum filter of mentioning in prior art can meet the present invention, without special combination, shape and functional requirement, as the GF type rotary drum vacuum filter of Shanghai chemical machinery Co., Ltd manufacture, also have disclosed vacuum-type drum filter in patent documentation CN201082371 can meet the present invention, the schematic diagram that vacuum-type drum filter shown in accompanying drawing just selects the structure of one of them to provide for demonstration structure of the present invention, do not there is special protection domain.
Innovation of the present invention is, at inner bottom part one sidewall of lautertuns, one supersonic generator 8 is installed, and at lautertuns one sidewall, is shaped with enzymolysis liquid entrance 5, and enzymolysis liquid entrance connects enzymolysis liquid front pump 6.
The enzymolysis liquid front pump that the present embodiment provides adopts motor 7 to drive, and is packed on support in motor one is logical.
What following examples adopted is Italian Padovan vacuum-type drum filter, is fixedly mounted with supersonic generator in lautertuns, at sidewall, is also shaped with enzymolysis liquid entrance.
Vacuum-type drum filter is processed a ultrafiltration tank bottoms processing method, and step is as follows:
Perlite 6kg(1.5 unit/kg), thick diatomite 20kg, thin diatomite 50kg (3.5 yuan/kg) (1) drum surface cloth soil: the rotary drum of vacuum-type drum filter is carried out to rotary drum and carry out cloth soil, cloth soil thickness 4cm, by soil amount:; Tank bottoms disposal ability: 206kg/h.m after cloth soil
2.Fruit juice flux: 157.5kg/h.m after cloth soil
2.Three kinds of soil is cycling coating in order repeatedly from inside to outside, the main fine earth that is coated with after 2.5-3cm, final coating layer thickness 4cm;
(2) after filling substrate being diluted with water, be placed in lautertuns, start agitating device, tank bottoms comprises the insoluble solids such as active carbon and fruit juice; Stir and open supersonic generator simultaneously, process 20-30 minute;
(3) pass into enzymolysis liquid, described enzymolysis liquid consists of: amylase, pectase, protease, cellulase, and its addition can regulate according to the content of insoluble solid in tank bottoms, and add and continue to stir 0.5-1 hour after enzymolysis liquid,
The addition of various enzymes is: amylase: diastatic addition is the 0.001-0.01% of tank bottoms weight, pectase: the addition of pectase is the 0.002-0.05% of tank bottoms weight, protease: the addition of protease is the 0.002-0.02% of tank bottoms weight; The addition of cellulase is the 0.002-0.05% of tank bottoms weight; Add the form of an enzymolysis liquid to add, the ratio of various enzymes can oneself regulate;
(4) led to after enzymolysis liquid and started drum drive unit, driven rotary drum to be rotated filtration, after filtering, active carbon is filtered to drum surface, when thickness to a certain extent after, with device for discharging, removed;
(5) the fruit juice that filters acquisition clings to and kills, and sterilization joins unified ultrafiltration and the subsequent step of carrying out in original fruit juice after the enzyme that goes out;
(6) the cloth of active carbon and drum surface soil one is logical removes as solid refuse, or after regeneration, continues to use.
The process of the test of the present embodiment and data analysis table
Interpretation of result:
1, this substandard cloth soil thickness 4cm, by soil amount: perlite 6kg(1.5 unit/kg), thick native 20kg, fine earth 50kg (3.5 yuan/kg), 254 yuan of cost accountings.
2, tank bottoms disposal ability: 206kg/h.m2 after cloth soil.
3, fruit juice flux: 157.5kg/h.m2 after cloth soil.
4, tank bottoms goes out juice pol 9
0bX, crushing juice rate 76.54%.
5, cross ultra-filtration flux 21.7kg/h.m2 for 16 ℃, (50 ℃, the normal fruit juice flux of 1kg pressure be 160kg/h.m2) flux is on the low side, analyzes relevant with fruit juice temperature and complicated composition.
6, concentrating sample indices is normal.
This tank bottoms process for producing line amount of water significantly reduces, and evaporimeter production capacity increases relatively, and pear juice is produced evaporimeter increases effective production time 3 hours, and production capacity increases by 17.7 tons every day; Sweet potato juice is produced evaporimeter increases effective production time 4 hours, and production capacity increases by 20 tons every day.Processor process tank substrate of the present invention is compared with water treatment before, by detailed calculating, can save tank bottom reason general expenses every day: when when pear juice is produced, 6143 yuan/day, sweet potato juice are produced 7293 yuan/day.
Claims (6)
1. process ultrafiltration tank bottoms Special vacuum rotary drum filter for one kind, comprise rotary drum driving device, lautertuns, rotary drum, dispensing head, agitating device, it is characterized in that: inner bottom part one sidewall at lautertuns is installed a supersonic generator, at lautertuns one sidewall, be shaped with enzymolysis liquid entrance, enzymolysis liquid entrance connects enzymolysis liquid front pump.
2. processing ultrafiltration tank bottoms Special vacuum rotary drum filter according to claim 1, is characterized in that: described enzymolysis liquid front pump adopts motor to drive.
3. employing vacuum-type drum filter is processed a ultrafiltration tank bottoms processing method, it is characterized in that: step is as follows:
(1) drum surface cloth is native: the rotary drum of vacuum-type drum filter is carried out to rotary drum and carry out cloth soil, cloth soil thickness 4cm, with native: perlite, thick soil, fine earth; Three kinds of soil is cycling coating in order repeatedly from inside to outside;
(2) after filling substrate being diluted with water, be placed in lautertuns, start agitating device, tank bottoms comprises the insoluble solids such as active carbon and fruit juice; Stir and open supersonic generator simultaneously, process 20-30 minute;
(3) pass into enzymolysis liquid, described enzymolysis liquid consists of: amylase, pectase, protease, cellulase, and its addition can regulate according to the content of insoluble solid in tank bottoms, and add and continue to stir 0.5-1 hour after enzymolysis liquid,
(4) led to after enzymolysis liquid and started drum drive unit, driven rotary drum to be rotated filtration, after filtering, active carbon is filtered to drum surface, when thickness to a certain extent after, with device for discharging, removed;
(5) the fruit juice that filters acquisition clings to and kills, and sterilization joins unified ultrafiltration and the subsequent step of carrying out in original fruit juice after the enzyme that goes out;
(6) the cloth of active carbon and drum surface soil one is logical removes as solid refuse.
4. employing vacuum-type drum filter according to claim 3 is processed ultrafiltration tank bottoms processing method, it is characterized in that: tank bottoms disposal ability: 206kg/h.m after described cloth soil
2, fruit juice flux: 157.5kg/h.m after cloth soil
2.
5. employing vacuum-type drum filter according to claim 3 is processed ultrafiltration tank bottoms processing method, it is characterized in that: during described cloth, after 2.5-3cm, be coated with fine earth, final coating layer thickness 4cm.
6. employing vacuum-type drum filter according to claim 3 is processed ultrafiltration tank bottoms processing method, it is characterized in that: in described enzymolysis liquid, the addition of various enzymes is: amylase: diastatic addition is the 0.001-0.01% of tank bottoms weight, pectase: the addition of pectase is the 0.002-0.05% of tank bottoms weight, protease: the addition of protease is the 0.002-0.02% of tank bottoms weight; The addition of cellulase is the 0.002-0.05% of tank bottoms weight.
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| CN201310481799.6A CN103520979B (en) | 2013-10-08 | 2013-10-15 | A kind of process ultrafiltration tank bottoms Special vacuum rotary drum filter and ultrafiltration tank bottoms processing method |
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| CN201310481799.6A CN103520979B (en) | 2013-10-08 | 2013-10-15 | A kind of process ultrafiltration tank bottoms Special vacuum rotary drum filter and ultrafiltration tank bottoms processing method |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104174203A (en) * | 2014-09-04 | 2014-12-03 | 南阳鑫子源石油石化技术装备有限公司 | Drum type mud press |
| CN104192937A (en) * | 2014-09-04 | 2014-12-10 | 南阳鑫子源石油石化技术装备有限公司 | Sludge-water separation drum |
| CN106721867A (en) * | 2015-11-24 | 2017-05-31 | 宜兴恒盛农业发展有限公司 | Ultrafiltration system is digested in a kind of cranberry juice production |
| CN109224625A (en) * | 2017-07-10 | 2019-01-18 | 新特能源股份有限公司 | For vacuum-type drum filter pre-filtering coating and its preparation process, processing production of polysilicon obtained in slurry technique |
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| CN102755777A (en) * | 2012-05-17 | 2012-10-31 | 南宁市甜蜜糖机设备分蜜机厂 | Filter cloth-free vacuum suction filter capable of bidirectionally sucking juice |
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| US2378237A (en) * | 1942-09-02 | 1945-06-12 | Wingfoot Corp | Method and apparatus for ultrasonic testing |
| US5785801A (en) * | 1996-05-08 | 1998-07-28 | Technimark, Inc. | Apparatus for covering a textile dye tube |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104174203A (en) * | 2014-09-04 | 2014-12-03 | 南阳鑫子源石油石化技术装备有限公司 | Drum type mud press |
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| CN106721867A (en) * | 2015-11-24 | 2017-05-31 | 宜兴恒盛农业发展有限公司 | Ultrafiltration system is digested in a kind of cranberry juice production |
| CN109224625A (en) * | 2017-07-10 | 2019-01-18 | 新特能源股份有限公司 | For vacuum-type drum filter pre-filtering coating and its preparation process, processing production of polysilicon obtained in slurry technique |
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| CN103520979B (en) | 2015-07-29 |
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Inventor after: Zhang Jiming Inventor after: Song Xinfei Inventor after: Wang Ying Inventor after: Wang Sixin Inventor after: Leng Chuanzhu Inventor after: Sun Yajun Inventor after: Li Xihong Inventor after: Li Yaoyao Inventor after: Jiang Nan Inventor after: Xu Ningzhou Inventor after: Yang Yaxu Inventor before: Wang Sixin Inventor before: Leng Chuanzhu Inventor before: Sun Yajun Inventor before: Li Xihong Inventor before: Li Yaoyao Inventor before: Jiang Nan Inventor before: Xu Ningzhou Inventor before: Yang Yaxu |
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Effective date of registration: 20160518 Address after: 100037 Beijing Fengtai District Branch Road No. 7 room 205 Patentee after: Guotouzhonglu Fruit Juice Co., Ltd. Patentee after: Rushan Zhongcheng fruit juice beverage Co., Ltd. Address before: 100037 Beijing Fengtai District Branch Road No. 7 room 205 Patentee before: Guotouzhonglu Fruit Juice Co., Ltd. |
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Effective date of registration: 20180821 Address after: 100037 room 205, 7 Kexing Road, Fengtai District, Beijing. Co-patentee after: Hebei Guo Zhong Lu fruit and vegetable juice Co., Ltd. Patentee after: Guotouzhonglu Fruit Juice Co., Ltd. Address before: 100037 room 205, 7 Kexing Road, Fengtai District, Beijing. Co-patentee before: Rushan Zhongcheng fruit juice beverage Co., Ltd. Patentee before: Guotouzhonglu Fruit Juice Co., Ltd. |