CN203360344U - Integrated system device for gardenia extract membrane separation - Google Patents
Integrated system device for gardenia extract membrane separation Download PDFInfo
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- CN203360344U CN203360344U CN 201320448228 CN201320448228U CN203360344U CN 203360344 U CN203360344 U CN 203360344U CN 201320448228 CN201320448228 CN 201320448228 CN 201320448228 U CN201320448228 U CN 201320448228U CN 203360344 U CN203360344 U CN 203360344U
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Abstract
The utility model discloses an integrated system device for gardenia extract membrane separation. The device comprises a purified water treatment system used for supplying water for production and cleaning of all systems, a macromolecular ultrafiltration membrane system, a micro-molecular concentration separation membrane system and a concentration membrane system; a discharge port of the macromolecular ultrafiltration membrane system is connected with a feed port of the micro-molecular concentration separation membrane system; and a discharge port of the micro-molecular concentration separation membrane system is connected with a feed port of the concentration membrane system. According to the device, production equipment is improved and optimized, an internal advanced nanometer membrane separation technology is taken as a core, and reasonable technical parameters (pressure, flow, flow velocity, temperature, PH and the like) suitable for product production are adopted, so that the whole product production is optimized; and the device has the characteristics that the occupied area is small, labor force and energy consumption are saved, the environment protection problem is solved, the product quality is improved, the product yield is increased, automatic control is realized, the operation is convenient, the service life is long, the operation cost is low, and the like.
Description
Technical field
The utility model relates to a kind of filtering separation system, relates in particular to a kind of Fructus Gardeniae extract membrane sepn integral system equipment.
Background technology
Separation of ethanol system of the prior art is in the extraction using alcohol process, larger to the consumption of ethanol, and production cost increases; Tap water or underground water lixiviate can be brought a large amount of heavy metal ion into, have affected quality product simultaneously; And separate Gardenia Yellow and jasminoidin for macroporous resin adsorption, adsorb not thorough, the resin regeneration technique complexity, absorb-elute is not thorough simultaneously, causes the loss of product, the yield reduction.And the resin consumption is large, cause the increase of production cost.Secondly the resin absorption quality product is lower, and wherein OD ratio is higher, higher than standard.Another kind, the mode of the concentrated jasminoidin of steam, steam consumption is large, and energy consumption is higher, and high temperature is concentrated that effective constituent is damaged, and reduces product yield.
The utility model content
The purpose of this utility model provides a kind of Fructus Gardeniae extract membrane sepn integral system equipment with regard to being in order to address the above problem.
The utility model is achieved through the following technical solutions above-mentioned purpose:
The utility model comprises for purified water treatment system, macromole ultrafiltration membrane system, small molecules concentrating and separating film system and the concentrated film system of each system production and water for cleaning are provided, the discharge port of described macromole ultrafiltration membrane system is connected with the opening for feed of described small molecules concentrating and separating film system, and the discharge port of described small molecules concentrating and separating film system is connected with the opening for feed of described concentrated film system.
Purified water treatment system described in the utility model comprises raw water box, pure water tank, cleaning case, pretreater, the low-pressure charging pump, high-pressure booster, scavenging pump, wet-pit, the pure water separating film module, magnetic valve, conductivity meter, the first flow meter, the second under meter, tensimeter before film, tensimeter after film, check valve, motor-driven control valve and valve, described valve comprises a plurality of, the water inlet of described raw water box is connected with tap water, the first water outlet of described raw water box is connected with the water inlet of described low-pressure charging pump by a described valve, the second water outlet of described raw water box connects a described valve as discharge outlet, the water outlet of described low-pressure charging pump is connected with the water inlet of described pretreater, the water outlet of described pretreater is connected with the water inlet of described high-pressure booster by a described valve, the water outlet of described high-pressure booster is connected with the water inlet of described check valve, the water outlet of described check valve connects by manometric water inlet before described film, the water outlet of described scavenging pump is connected with manometric water inlet before described film by a described valve, the water inlet of described pure water separating film module is connected with manometric water outlet before described film, the water inlet of described scavenging pump is connected with the first water outlet of described cleaning case by a described valve, the second water outlet of described cleaning case connects a described valve as discharge outlet, the first water outlet of described pure water separating film module is connected with the water inlet of described first flow meter by described conductivity meter, the second water outlet of described pure water separating film module simultaneously with described film after tensimeter, the water inlet of described magnetic valve, the water inlet of described motor-driven control valve connects, the second water outlet of described pure water separating film module also is connected with the water inlet of described cleaning case by a described valve, the water outlet of described motor-driven control valve is connected with the water inlet of described the second under meter, the water outlet of described first flow meter is connected with the water inlet of three described valves simultaneously, the water outlet of first described valve is the sampling discharge outlet, the water outlet of second described valve is connected with the first water inlet of described cleaning case, the water outlet of the 3rd described valve is connected with the water inlet of described pure water tank, the first water outlet of described pure water tank is connected with the water inlet of described wet-pit by a described valve, it after the second water outlet of described pure water tank is connected with a described bleed valve, is the pure water tank discharge outlet.
Macromole ultrafiltration membrane system described in the utility model comprises cape jasmine stoste case, the ultrafiltration membrane system topping-up pump, tensimeter before the ultrafiltration membrane system film, tensimeter after the ultrafiltration membrane system film, the ultrafiltration membrane system filter membrane component, ultrafiltration membrane system first flow meter, ultrafiltration membrane system the second under meter, ultrafiltration membrane system motor-driven control valve and thermometer, the feeding mouth of described cape jasmine stoste case is the gardenia extract entrance, the discharge port of described cape jasmine stoste case is connected with the feeding mouth of two described valves simultaneously, the discharge port of one of them described valve is cape jasmine stoste discharge outlet, the discharge port of another described valve is connected with the feeding mouth of described ultrafiltration membrane system topping-up pump, the discharge port of described ultrafiltration membrane system topping-up pump successively with described ultrafiltration membrane system film before tensimeter, described thermometer, the feeding mouth of described ultrafiltration membrane system filter membrane component is connected with the feeding mouth of a described valve, the first discharge port of described ultrafiltration membrane system filter membrane component is connected with the feeding mouth of described ultrafiltration membrane system first flow meter, the discharge port of described ultrafiltration membrane system first flow meter is connected with the feeding mouth of three described valves simultaneously, the discharge port of one of them described valve is the sampling discharge outlet, the discharge port that the discharge port of second described valve is described macromole ultrafiltration membrane system, the discharge port of the 3rd described valve is connected with the feeding mouth of described cape jasmine stoste case, the second discharging of described ultrafiltration membrane system by described ultrafiltration membrane system film after tensimeter with after a described valve, with the feeding mouth of described ultrafiltration membrane system the second under meter, be connected, the discharge port of described ultrafiltration membrane system the second under meter is connected with the second feeding mouth of described cape jasmine stoste case.
Small molecules concentrating and separating film system described in the utility model comprises clarification gardenia extract storage tank, the separation membrane system high-pressure pump, tensimeter before the separation membrane system film, tensimeter after the separation membrane system film, the separation membrane system check valve, the separation membrane system thermometer, the separation membrane system filter membrane component, the separation membrane system motor-driven control valve, separation membrane system first flow meter and separation membrane system the second under meter, the discharge port of described clarification gardenia extract storage tank is connected with the feeding mouth of two described valves simultaneously, the discharge port of one of them described valve is the gardenin concentrated solution outlet, the discharge port of another described valve is connected with the feeding mouth of described separation membrane system high-pressure pump, the discharge port of described separation membrane system high-pressure pump successively with described separation membrane system check valve, tensimeter before described separation membrane system film, the separation membrane system thermometer is connected with the feeding mouth of described separation membrane system filter membrane component, the first discharge port of described separation membrane system filter membrane component is connected with the feeding mouth of described separation membrane system first flow meter, the discharge port of described separation membrane system first flow meter is connected with the feeding mouth of three described valves simultaneously, the discharge port of one of them described valve is separation membrane system sampling discharge outlet, the discharge port that the discharge port of second described valve is described small molecules concentrating and separating film system, the discharge port of the 3rd described valve is connected with the feeding mouth of described clarification gardenia extract storage tank, the second discharge port of described separation membrane system filter membrane component is connected with manometric feeding mouth after described separation membrane system film with the feeding mouth of a described valve simultaneously, after described separation membrane system film, manometric discharge port is connected with the feeding mouth of described separation membrane system motor-driven control valve, the discharge port of described separation membrane system motor-driven control valve is connected with the feeding mouth of described separation membrane system the second under meter, the discharge port of described separation membrane system the second under meter is connected with the feeding mouth of described clarification gardenia extract storage tank.
Concentrated film system described in the utility model comprises the jasminoidin storage tank, concentrated film system high pressure pump, concentrated film system one way valve, tensimeter before concentrated film system membranes, tensimeter after concentrated film system membranes, concentrated film system temperature meter, concentrated film system filter membrane component, concentrated film system first flow meter, concentrated film system the second under meter, concentrated film system motor-driven control valve, see through liquid storage tank and concentrated film system emptying pump, the discharge port of described jasminoidin storage tank is connected with the feeding mouth of two described valves simultaneously, the discharge port of one of them described valve is jasminoidin concentrated solution discharge outlet, the discharge port of another described valve is connected with the feeding mouth of described concentrated film system high pressure pump, the discharge port of described concentrated film system high pressure pump successively with described concentrated film system one way valve, tensimeter before described concentrated film system membranes, concentrated film system temperature meter is connected with the feeding mouth of described concentrated film system filter membrane component, the discharge port of described concentrated film system first flow meter is connected with the feeding mouth of three described valves simultaneously, the discharge port of one of them described valve is concentrated film system sampling discharge outlet, the discharge port of second described valve is connected with the described feeding mouth that sees through liquid storage tank, the discharge port of the 3rd described valve is connected with the feeding mouth of described jasminoidin storage tank, the second discharge port of described concentrated film system filter membrane component is connected with manometric feeding mouth after described concentrated film system membranes with a described valve simultaneously, after described concentrated film system membranes, manometric discharge port is connected with the feeding mouth of described concentrated film system motor-driven control valve, the discharge port of described concentrated film system motor-driven control valve is connected with the feeding mouth of concentrated film system the second under meter, the discharge port of described concentrated film system the second under meter is connected with the feeding mouth of described jasminoidin storage tank, described the first discharge port that sees through liquid storage tank is connected with the feeding mouth of described concentrated film system emptying pump by a described valve, the discharge port that the discharge port of described concentrated film system emptying pump is described concentrated film system.
The beneficial effects of the utility model are:
The utility model water carries out the extraction of cape jasmine fruit, and at first integrated system is processed former water, and the water quality standard after processing reaches national medical standard one-level purified water standard, thereby has avoided the impact of raw water quality on quality product; Secondly Gardenia Yellow and the jasminoidin solution of water extraction are carried out to the removal of impurities processing, remove the macromole impurity (colloidalmaterial, albumen etc.) in solution; Again Gardenia Yellow and jasminoidin being carried out to the physical compression formula separates, by distinguishing of two kinds of material sizes sieved, do not add anything, do not adopt absorption yet, flash liberation makes 0D ratio lower than 0.2, meets target level of product quality, and sepn process is carried out concentrated process to Gardenia Yellow simultaneously, normal temperature is realized concentrated, has saved energy consumption; Finally the jasminoidin solution of after separating carried out to normal temperature physics thickening processing, effectively guaranteed quality product, concentrated water outlet qualified discharge, realize the requirement of energy-saving and emission-reduction simultaneously.Mainly solve the extraction Solvent (ethanol in original production process, tap water, underground water), the technological process of production is simplified and optimized simultaneously, production unit is improved and optimized, adopting international advanced nanometer film isolation technique is core, adopt the technical matters parameter (pressure that rationally is appropriate to this products production, flow, flow velocity, temperature, PH etc.), whole products production is optimized, and it is little to the utlity model has occupation of land, saved the labor force, save energy consumption, solve the difficult problem of environmental protection, improve the quality of products, improve product yield, automatization is controlled, easy to operate, long service life, the characteristics such as running cost is low.
The accompanying drawing explanation
Fig. 1 is the structural representation of purified water treatment system described in the utility model;
Fig. 2 is the structural representation of macromole ultrafiltration membrane system described in the utility model;
Fig. 3 is the structural representation of small molecules concentrating and separating film system described in the utility model;
Fig. 4 is the structural representation of concentrated film system described in the utility model.
In figure: the 1-cleaning case, the 2-raw water box, 3-low-pressure charging pump, the 4-scavenging pump, the 5-pretreater, the 6-high-pressure booster, the 7-check valve, tensimeter before the 8-film, 9-pure water separating film module, tensimeter after the 10-film, the 11-magnetic valve, the 12-motor-driven control valve, 13-the second under meter, the 14-conductivity meter, 15-first flow meter, the 16-pure water tank, the 17-wet-pit, 21-cape jasmine stoste case, 22-ultrafiltration membrane system the second under meter, 23-ultrafiltration membrane system motor-driven control valve, tensimeter after 24-ultrafiltration membrane system film, 25-ultrafiltration membrane system first flow meter, 26-ultrafiltration membrane system topping-up pump, tensimeter before 27-ultrafiltration membrane system film, the 28-thermometer, 29-ultrafiltration membrane system filter membrane component, 31-clarification gardenia extract storage tank, 32-separation membrane system the second under meter, 33-separation membrane system motor-driven control valve, tensimeter after 34-separation membrane system film, 35-separation membrane system high-pressure pump, 36-separation membrane system filter membrane component, 37-separation membrane system thermometer, 38-separation membrane system check valve, tensimeter before 39-separation membrane system film, 311-separation membrane system first flow meter, 41-jasminoidin storage tank, 42-concentrates film system the second under meter, 43-concentrates film system motor-driven control valve, tensimeter after the concentrated film system membranes of 44-, 45-concentrates film system high pressure pump, 46-concentrates film system temperature meter, 47-concentrates film system filter membrane component, 48-concentrates the film system one way valve, tensimeter before the concentrated film system membranes of 49-, 410-concentrates film system emptying pump, 411-concentrates film system first flow meter, 412-sees through liquid storage tank.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail:
The utility model comprises for purified water treatment system, macromole ultrafiltration membrane system, small molecules concentrating and separating film system and the concentrated film system of each system production and water for cleaning are provided, the discharge port of described macromole ultrafiltration membrane system is connected with the opening for feed of described small molecules concentrating and separating film system, and the discharge port of described small molecules concentrating and separating film system is connected with the opening for feed of described concentrated film system.
As shown in Figure 1: the utility model purified water treatment system comprises raw water box 2, pure water tank 16, cleaning case 1, pretreater 5, low-pressure charging pump 3, high-pressure booster 6, scavenging pump 1, wet-pit 17, pure water separating film module 9, magnetic valve 11, conductivity meter 14, first flow meter 15, the second under meter 13, tensimeter 8 before film, after film, tensimeter 10, check valve 7, motor-driven control valve 12 and valve, valve comprises a plurality of, the water inlet of raw water box 2 is connected with tap water, the first water outlet of raw water box 2 is connected with the water inlet of low-pressure charging pump 3 by a valve, the second water outlet of raw water box 2 connects a valve as discharge outlet, the water outlet of low-pressure charging pump 3 is connected with the water inlet of pretreater 5, the water outlet of pretreater 5 is connected with the water inlet of high-pressure booster 6 by a valve, the water outlet of high-pressure booster 6 is connected with the water inlet of check valve 7, the water outlet of check valve 7 connects by the water inlet of tensimeter 8 before film, the water outlet of scavenging pump 4 is connected with the water inlet of tensimeter 8 before film by a valve, the water inlet of pure water separating film module 9 is connected with the water outlet of tensimeter 8 before film, the water inlet of scavenging pump 4 is connected with the first water outlet of cleaning case 1 by a valve, the second water outlet of cleaning case 1 connects a valve as discharge outlet, the first water outlet of pure water separating film module 9 is connected with the water inlet of first flow meter by conductivity meter 14, the second water outlet of pure water separating film module 9 simultaneously with film after tensimeter 10, the water inlet of magnetic valve 11, the water inlet of motor-driven control valve 12 connects, the second water outlet of pure water separating film module 9 also is connected with the water inlet of cleaning case 1 by a valve, the water outlet of motor-driven control valve 12 is connected with the water inlet of the second under meter 13, the water outlet of first flow meter 15 is connected with the water inlet of three valves simultaneously, the water outlet of first valve is the sampling discharge outlet, the water outlet of second valve is connected with the first water inlet of cleaning case 1, the water outlet of the 3rd valve is connected with the water inlet of pure water tank 16, the first water outlet of pure water tank 16 is connected with the water inlet of wet-pit 17 by a valve, it after the second water outlet of pure water tank 16 is connected with a bleed valve, is the pure water tank discharge outlet.
As shown in Figure 2: the utility model macromole ultrafiltration membrane system comprises cape jasmine stoste case 21, ultrafiltration membrane system topping-up pump 26, tensimeter 27 before the ultrafiltration membrane system film, after the ultrafiltration membrane system film, tensimeter 24, ultrafiltration membrane system filter membrane component 29, ultrafiltration membrane system first flow meter 25, ultrafiltration membrane system the second under meter 22, ultrafiltration membrane system motor-driven control valve 23 and thermometer 28, the feeding mouth of cape jasmine stoste case 21 is the gardenia extract entrance, the discharge port of cape jasmine stoste case 21 is connected with the feeding mouth of two valves simultaneously, the discharge port of one of them valve is cape jasmine stoste discharge outlet, the discharge port of another valve is connected with the feeding mouth of ultrafiltration membrane system topping-up pump 26, the discharge port of ultrafiltration membrane system topping-up pump 26 successively with the ultrafiltration membrane system film before tensimeter 27, thermometer 28, the feeding mouth of ultrafiltration membrane system filter membrane component 29 is connected with the feeding mouth of a valve, the first discharge port of ultrafiltration membrane system filter membrane component 29 is connected with the feeding mouth of ultrafiltration membrane system first flow meter 25, the discharge port of ultrafiltration membrane system first flow meter 25 is connected with the feeding mouth of three valves simultaneously, the discharge port of one of them valve is the sampling discharge outlet, the discharge port that the discharge port of second valve is the macromole ultrafiltration membrane system, the discharge port of the 3rd valve is connected with the feeding mouth of cape jasmine stoste case 21, the second discharging of ultrafiltration membrane system by tensimeter 24 after the ultrafiltration membrane system film with after a valve, with the feeding mouth of ultrafiltration membrane system the second under meter 22, be connected, the discharge port of ultrafiltration membrane system the second under meter 22 is connected with the second feeding mouth of cape jasmine stoste case 21.
As shown in Figure 3: the utility model small molecules concentrating and separating film system comprises clarification gardenia extract storage tank 31, separation membrane system high-pressure pump 32, tensimeter 39 before the separation membrane system film, after the separation membrane system film, tensimeter 34, separation membrane system check valve 38, separation membrane system thermometer 37, separation membrane system filter membrane component 36, separation membrane system motor-driven control valve 33, separation membrane system first flow meter 311 and separation membrane system the second under meter 32, the discharge port of clarification gardenia extract storage tank 31 is connected with the feeding mouth of two valves simultaneously, the discharge port of one of them valve is the gardenin concentrated solution outlet, the discharge port of another valve is connected with the feeding mouth of separation membrane system high-pressure pump 35, the discharge port of separation membrane system high-pressure pump 35 successively with separation membrane system check valve 38, tensimeter 39 before the separation membrane system film, separation membrane system thermometer 37 is connected with the feeding mouth of separation membrane system filter membrane component 36, the first discharge port of separation membrane system filter membrane component 36 is connected with the feeding mouth of separation membrane system first flow meter 311, the discharge port of separation membrane system first flow meter 311 is connected with the feeding mouth of three valves simultaneously, the discharge port of one of them valve is separation membrane system sampling discharge outlet, the discharge port that the discharge port of second valve is small molecules concentrating and separating film system, the discharge port of the 3rd valve is connected with the feeding mouth of clarification gardenia extract storage tank 31, the second discharge port of separation membrane system filter membrane component 36 is connected with the feeding mouth of tensimeter 34 after the separation membrane system film with the feeding mouth of a valve simultaneously, after the separation membrane system film, the discharge port of tensimeter 34 is connected with the feeding mouth of separation membrane system motor-driven control valve 33, the discharge port of separation membrane system motor-driven control valve 33 is connected with the feeding mouth of separation membrane system the second under meter 32, the discharge port of separation membrane system the second under meter 32 is connected with the feeding mouth of clarification gardenia extract storage tank 31.
As shown in Figure 4: the concentrated film system of the utility model comprises jasminoidin storage tank 41, concentrated film system high pressure pump 45, concentrated film system one way valve 48, tensimeter 49 before concentrated film system membranes, tensimeter 44 after concentrated film system membranes, concentrated film system temperature meter 46, concentrated film system filter membrane component 47, concentrated film system first flow meter 411, concentrated film system the second under meter 42, concentrated film system motor-driven control valve 43, see through liquid storage tank 412 and concentrated film system emptying pump 410, the discharge port of jasminoidin storage tank 41 is connected with the feeding mouth of two valves simultaneously, the discharge port of one of them valve is jasminoidin concentrated solution discharge outlet, the discharge port of another valve is connected with the feeding mouth of concentrated film system high pressure pump 45, the discharge port of concentrated film system high pressure pump 45 successively with concentrated film system one way valve 48, tensimeter 49 before concentrated film system membranes, concentrated film system temperature meter 46 is connected with the feeding mouth of concentrated film system filter membrane component 47, the discharge port of concentrated film system first flow meter 411 is connected with the feeding mouth of three valves simultaneously, the discharge port of one of them valve is concentrated film system sampling discharge outlet, the discharge port of second valve is connected with the feeding mouth that sees through liquid storage tank 412, the discharge port of the 3rd valve is connected with the feeding mouth of jasminoidin storage tank 41, the second discharge port of concentrated film system filter membrane component 47 is connected with the feeding mouth of tensimeter 44 after concentrated film system membranes with a valve simultaneously, after concentrated film system membranes, the discharge port of tensimeter 44 is connected with the feeding mouth of concentrated film system motor-driven control valve 43, the discharge port of concentrated film system motor-driven control valve 43 is connected with the feeding mouth of concentrated film system the second under meter 42, the discharge port of concentrated film system the second under meter 42 is connected with the feeding mouth of jasminoidin storage tank 41, the first discharge port that sees through liquid storage tank 412 is connected with the feeding mouth of concentrated film system emptying pump 410 by a valve, the discharge port of concentrated film system emptying pump 410 is the discharge port of concentrated film system.
As shown in Figure 1, Figure 2, Figure 3 and Figure 4: by ultrafiltration membrane system topping-up pump 26, the jasminoidin solution of separator well is pumped into to ultrafiltration membrane system filter membrane component 29 and circulate concentrated, clear water appears the system discharge, jasminoidin is trapped, reach concentrated purpose, pass through the rotating speed of variable frequency adjustment pump in process, the regulation system operating pressure, tensimeter, the under meter in each system detected system parameter simultaneously, and system temperature is controlled the bronze drum interchanger and is regulated.By above four membrane sepn integral system equipments, Fructus Gardeniae extract is effectively extracted, separates concentrated Gardenia Yellow, concentrated jasminoidin, reached improve product yield, improve the quality of products, energy-saving and emission-reduction, cleaner production, the effect that reduces production costs.
Claims (5)
1. a Fructus Gardeniae extract membrane sepn integral system equipment, it is characterized in that: comprise for purified water treatment system, macromole ultrafiltration membrane system, small molecules concentrating and separating film system and the concentrated film system of each system production and water for cleaning are provided, the discharge port of described macromole ultrafiltration membrane system is connected with the opening for feed of described small molecules concentrating and separating film system, and the discharge port of described small molecules concentrating and separating film system is connected with the opening for feed of described concentrated film system.
2. Fructus Gardeniae extract membrane sepn integral system equipment according to claim 1, it is characterized in that: described purified water treatment system comprises raw water box, pure water tank, cleaning case, pretreater, the low-pressure charging pump, high-pressure booster, scavenging pump, wet-pit, the pure water separating film module, magnetic valve, conductivity meter, the first flow meter, the second under meter, tensimeter before film, tensimeter after film, check valve, motor-driven control valve and valve, described valve comprises a plurality of, the water inlet of described raw water box is connected with tap water, the first water outlet of described raw water box is connected with the water inlet of described low-pressure charging pump by a described valve, the second water outlet of described raw water box connects a described valve as discharge outlet, the water outlet of described low-pressure charging pump is connected with the water inlet of described pretreater, the water outlet of described pretreater is connected with the water inlet of described high-pressure booster by a described valve, the water outlet of described high-pressure booster is connected with the water inlet of described check valve, the water outlet of described check valve connects by manometric water inlet before described film, the water outlet of described scavenging pump is connected with manometric water inlet before described film by a described valve, the water inlet of described pure water separating film module is connected with manometric water outlet before described film, the water inlet of described scavenging pump is connected with the first water outlet of described cleaning case by a described valve, the second water outlet of described cleaning case connects a described valve as discharge outlet, the first water outlet of described pure water separating film module is connected with the water inlet of described first flow meter by described conductivity meter, the second water outlet of described pure water separating film module simultaneously with described film after tensimeter, the water inlet of described magnetic valve, the water inlet of described motor-driven control valve connects, the second water outlet of described pure water separating film module also is connected with the water inlet of described cleaning case by a described valve, the water outlet of described motor-driven control valve is connected with the water inlet of described the second under meter, the water outlet of described first flow meter is connected with the water inlet of three described valves simultaneously, the water outlet of first described valve is the sampling discharge outlet, the water outlet of second described valve is connected with the first water inlet of described cleaning case, the water outlet of the 3rd described valve is connected with the water inlet of described pure water tank, the first water outlet of described pure water tank is connected with the water inlet of described wet-pit by a described valve, it after the second water outlet of described pure water tank is connected with a described bleed valve, is the pure water tank discharge outlet.
3. Fructus Gardeniae extract membrane sepn integral system equipment according to claim 1, it is characterized in that: described macromole ultrafiltration membrane system comprises cape jasmine stoste case, the ultrafiltration membrane system topping-up pump, tensimeter before the ultrafiltration membrane system film, tensimeter after the ultrafiltration membrane system film, the ultrafiltration membrane system filter membrane component, ultrafiltration membrane system first flow meter, ultrafiltration membrane system the second under meter, ultrafiltration membrane system motor-driven control valve and thermometer, the feeding mouth of described cape jasmine stoste case is the gardenia extract entrance, the discharge port of described cape jasmine stoste case is connected with the feeding mouth of two described valves simultaneously, the discharge port of one of them described valve is cape jasmine stoste discharge outlet, the discharge port of another described valve is connected with the feeding mouth of described ultrafiltration membrane system topping-up pump, the discharge port of described ultrafiltration membrane system topping-up pump successively with described ultrafiltration membrane system film before tensimeter, described thermometer, the feeding mouth of described ultrafiltration membrane system filter membrane component is connected with the feeding mouth of a described valve, the first discharge port of described ultrafiltration membrane system filter membrane component is connected with the feeding mouth of described ultrafiltration membrane system first flow meter, the discharge port of described ultrafiltration membrane system first flow meter is connected with the feeding mouth of three described valves simultaneously, the discharge port of one of them described valve is the sampling discharge outlet, the discharge port that the discharge port of second described valve is described macromole ultrafiltration membrane system, the discharge port of the 3rd described valve is connected with the feeding mouth of described cape jasmine stoste case, the second discharging of described ultrafiltration membrane system by described ultrafiltration membrane system film after tensimeter with after a described valve, with the feeding mouth of described ultrafiltration membrane system the second under meter, be connected, the discharge port of described ultrafiltration membrane system the second under meter is connected with the second feeding mouth of described cape jasmine stoste case.
4. Fructus Gardeniae extract membrane sepn integral system equipment according to claim 1, it is characterized in that: described small molecules concentrating and separating film system comprises clarification gardenia extract storage tank, the separation membrane system high-pressure pump, tensimeter before the separation membrane system film, tensimeter after the separation membrane system film, the separation membrane system check valve, the separation membrane system thermometer, the separation membrane system filter membrane component, the separation membrane system motor-driven control valve, separation membrane system first flow meter and separation membrane system the second under meter, the discharge port of described clarification gardenia extract storage tank is connected with the feeding mouth of two described valves simultaneously, the discharge port of one of them described valve is the gardenin concentrated solution outlet, the discharge port of another described valve is connected with the feeding mouth of described separation membrane system high-pressure pump, the discharge port of described separation membrane system high-pressure pump successively with described separation membrane system check valve, tensimeter before described separation membrane system film, the separation membrane system thermometer is connected with the feeding mouth of described separation membrane system filter membrane component, the first discharge port of described separation membrane system filter membrane component is connected with the feeding mouth of described separation membrane system first flow meter, the discharge port of described separation membrane system first flow meter is connected with the feeding mouth of three described valves simultaneously, the discharge port of one of them described valve is separation membrane system sampling discharge outlet, the discharge port that the discharge port of second described valve is described small molecules concentrating and separating film system, the discharge port of the 3rd described valve is connected with the feeding mouth of described clarification gardenia extract storage tank, the second discharge port of described separation membrane system filter membrane component is connected with manometric feeding mouth after described separation membrane system film with the feeding mouth of a described valve simultaneously, after described separation membrane system film, manometric discharge port is connected with the feeding mouth of described separation membrane system motor-driven control valve, the discharge port of described separation membrane system motor-driven control valve is connected with the feeding mouth of described separation membrane system the second under meter, the discharge port of described separation membrane system the second under meter is connected with the feeding mouth of described clarification gardenia extract storage tank.
5. Fructus Gardeniae extract membrane sepn integral system equipment according to claim 1, it is characterized in that: described concentrated film system comprises the jasminoidin storage tank, concentrated film system high pressure pump, concentrated film system one way valve, tensimeter before concentrated film system membranes, tensimeter after concentrated film system membranes, concentrated film system temperature meter, concentrated film system filter membrane component, concentrated film system first flow meter, concentrated film system the second under meter, concentrated film system motor-driven control valve, see through liquid storage tank and concentrated film system emptying pump, the discharge port of described jasminoidin storage tank is connected with the feeding mouth of two described valves simultaneously, the discharge port of one of them described valve is jasminoidin concentrated solution discharge outlet, the discharge port of another described valve is connected with the feeding mouth of described concentrated film system high pressure pump, the discharge port of described concentrated film system high pressure pump successively with described concentrated film system one way valve, tensimeter before described concentrated film system membranes, concentrated film system temperature meter is connected with the feeding mouth of described concentrated film system filter membrane component, the discharge port of described concentrated film system first flow meter is connected with the feeding mouth of three described valves simultaneously, the discharge port of one of them described valve is concentrated film system sampling discharge outlet, the discharge port of second described valve is connected with the described feeding mouth that sees through liquid storage tank, the discharge port of the 3rd described valve is connected with the feeding mouth of described jasminoidin storage tank, the second discharge port of described concentrated film system filter membrane component is connected with manometric feeding mouth after described concentrated film system membranes with a described valve simultaneously, after described concentrated film system membranes, manometric discharge port is connected with the feeding mouth of described concentrated film system motor-driven control valve, the discharge port of described concentrated film system motor-driven control valve is connected with the feeding mouth of concentrated film system the second under meter, the discharge port of described concentrated film system the second under meter is connected with the feeding mouth of described jasminoidin storage tank, described the first discharge port that sees through liquid storage tank is connected with the feeding mouth of described concentrated film system emptying pump by a described valve, the discharge port that the discharge port of described concentrated film system emptying pump is described concentrated film system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320448228 CN203360344U (en) | 2013-07-26 | 2013-07-26 | Integrated system device for gardenia extract membrane separation |
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| CN 201320448228 CN203360344U (en) | 2013-07-26 | 2013-07-26 | Integrated system device for gardenia extract membrane separation |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103735633A (en) * | 2013-12-30 | 2014-04-23 | 南京博士牛生物科技有限公司 | Preparation method of instant gardenia powder |
| CN108976842A (en) * | 2018-07-05 | 2018-12-11 | 成都和诚过滤技术有限公司 | Gardenia Yellow extraction process by water |
-
2013
- 2013-07-26 CN CN 201320448228 patent/CN203360344U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103735633A (en) * | 2013-12-30 | 2014-04-23 | 南京博士牛生物科技有限公司 | Preparation method of instant gardenia powder |
| CN103735633B (en) * | 2013-12-30 | 2016-01-20 | 南京博士牛生物科技有限公司 | A kind of preparation method of instant gardenia powder |
| CN108976842A (en) * | 2018-07-05 | 2018-12-11 | 成都和诚过滤技术有限公司 | Gardenia Yellow extraction process by water |
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