CN106731492A - The processing method of waste gas in a kind of Olive leaf P.E production - Google Patents
The processing method of waste gas in a kind of Olive leaf P.E production Download PDFInfo
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- CN106731492A CN106731492A CN201611079570.XA CN201611079570A CN106731492A CN 106731492 A CN106731492 A CN 106731492A CN 201611079570 A CN201611079570 A CN 201611079570A CN 106731492 A CN106731492 A CN 106731492A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1406—Multiple stage absorption
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1493—Selection of liquid materials for use as absorbents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/30—Loose or shaped packing elements, e.g. Raschig rings or Berl saddles, for pouring into the apparatus for mass or heat transfer
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2252/00—Absorbents, i.e. solvents and liquid materials for gas absorption
- B01D2252/10—Inorganic absorbents
- B01D2252/103—Water
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/30—Details relating to random packing elements
- B01J2219/302—Basic shape of the elements
- B01J2219/30207—Sphere
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/30—Details relating to random packing elements
- B01J2219/304—Composition or microstructure of the elements
- B01J2219/30441—Wood
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/30—Details relating to random packing elements
- B01J2219/304—Composition or microstructure of the elements
- B01J2219/30483—Fibrous materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/30—Details relating to random packing elements
- B01J2219/318—Manufacturing aspects
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- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
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- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Organic Chemistry (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses the processing method of waste gas in a kind of production of Olive leaf P.E, comprise the following steps:1) spray column absorbs:Enter spray column treatment after in the exhaust gas centralized that will be produced in production;Spray column is the two-stage of series connection, and built with filler, the liquid phase substance in spray column is water to two-stage spray column, and two grades of spray columns shield, and is coupled with subsequent technique treatment;2) gas that treatment is completed is by pipeline to factory's inner chimney high altitude discharge.
Description
Technical field
The present invention relates to technical field of waste gas treatment, the treatment of waste gas in more particularly to a kind of Olive leaf P.E production
Method.
Background technology
Olive (Olea europaea L.), is Oleaceae (Oleaceae) also known as olive, Europe olive, olive
Olea (Olea L) plant.Olive is the conventional medicament of Mediterranean Region, is used to treat various with leaf and fruit medicine
Disease.The decoction or preserved material of olive leaf, frequently as the medication among the people of diabetes, there is certain curative effect in mediterranean country.Olive
Leaf extract is used as dietary supplements to strengthen immunologic function in America and Europe.Modern data shows that olive has anti-heart rate
Uneven, antimycotic, anti-high cholesterol, hypoglycemic, hypotensive, anti-inflammatory is anti-oxidant, antiviral, diuresis, spasmolysis and vasodilation etc.
The various pharmacological activity of central nervous system, for treating diabetes, hypertension, diarrhoea, oedema, stomach angina, lump rash, respiratory tract
The diseases such as infection, constipation, urinary tract infection.Isolated chemical composition can be divided into from olive growing leaves:Flavonoids, driffractive ring alkene ether
Terpene, carbohydrate, organic acid and other compounds.Extractive of olive growing leaves have reduce blood sugar, reduction blood fat, bacteriostatic activity,
Antioxidation activity, anti-inflammatory activity strengthen many middle functions such as immune and beauty, and potentiality to be exploited is huge.Modern biotechnology analytical table
Bright, active material mainly has olive polyphenol, flavonoids, secoiridoid (including Cleupin) etc. in olive growing leaves, and
Its antioxidation biology active matter content is higher than olea europaea fruit and stem.
The plant cell of olive leaf is contained within grease, mainly by composition for triglycerides compound group into mixture,
These greases irregularly disperse with elaioleucite and oil body protoplast form, in discontinuous graininess, together with granule protein body
Existence form is present in the cell etc..Existing extracting method, is passed through after directly the raw materials such as olive leaf are smashed or crushed
The mode such as water extraction/alcohol extracting or Microwave Extraction is directly extracted, and when extracting, the grease in cell can be isolated simultaneously, oil
Fat in process of production, can ferment, decompose, and produce substantial amounts of gas, in these gases containing fragrant hydrocarbon system, styrene, hydro carbons,
The materials such as phenols, also with stench, if unprocessed just direct discharge, can cause workshop and neighboring area environment extremely to dislike
It is bad.In the prior art, Chinese patent CN104524946A, the processing method of waste gas in a kind of peony extract production, using 1)
Sub-cooled:Feeding low-temperature condenser carries out sub-cooled after in the exhaust gas centralized produced in production, and chilling temperature is 0-4 DEG C, real
The initial gross separation of essential oil in existing waste gas, essential oil enters low-temperature storage tank;2) spray column absorbs:Step 1) waste gas out enters spray
Tower treatment;Spray column be series connection level Four, the liquid phase substance in level Four spray column be respectively with the addition of xanthans concentration it is relatively low
Alkali lye, with the addition of the concentration of xanthans alkali lye higher, with the addition of the concentration of xanthans alkali lye and water higher;3) idle discharge high
Put:The gas for completing is processed by pipeline to factory's inner chimney high altitude discharge.Such processing method, for peony extract
The treatment of waste gas in production, preferably, but for the treatment of foul waste gas in Olive leaf P.E production, then effect difference is strong for effect
People's will, therefore, the Olive leaf P.E production waste gas containing foul smelling how is processed, it is a technical barrier.
The content of the invention
The purpose of the present invention is to solve the shortcomings of the prior art, there is provided the place of waste gas in a kind of Olive leaf P.E production
Reason method, can effectively purify the waste gas produced in olive leaf extraction process, and effect is obvious.
The processing method of waste gas, is achieved through the following technical solutions in a kind of Olive leaf P.E production, including following step
Suddenly:
1) spray column absorbs:Enter spray column treatment after in the exhaust gas centralized that will be produced in production;
Spray column is the two-stage of series connection, and built with filler, the liquid phase substance in spray column is water, two grades of sprays to two-stage spray column
Drench tower to shield, and couple with subsequent technique treatment;
2) gas that treatment is completed is by pipeline to factory's inner chimney high altitude discharge;
Described filler is prepared by the following method:
A, raw material prepare:Prepare filament, litchi rind;
The treatment of b, litchi rind:
1. pulverization process:Crush or the pure water equivalent to litchi rind 8-10 weight is added after smashing, with high speed shear breast
The treatment of change machine, is then processed with high pressure microjet Ultra-Micro Grinding Equipment in 25 DEG C, and processing pressure is 50-60MPa, treatment time
Number is 2-3 times, obtains paste serous material;
2. steam blasting:The material that 1. step obtains is put into steam blasting tank, burst pressure 3.0-3.5Mpa, during pressurize
Between maintain 150-200s;
3. decoct, decolourize:The pure water of the weights such as the material addition that 2. step is obtained is decocted 2 times, 1 hour every time, is obtained
Extract solution, filtering merges extract solution, and the medicinal extract that relative density is 1.30 is surveyed when filtrate is concentrated into 70 DEG C, dries, and sieving obtains powder
End;
C, by filament bunchy, make fibre bundle clamp stretch;Fibre bundle is spaced fusing with ultrasonic bonding head and forms molten
Node, the litchi rind powder for adding step b to obtain while fusing, is conveyed the good fibre bundle of clinkering by transmission device;Use knife
Piece carries out cutting the fiberfill to form same size, and launching fibre bundle as constraint point with the clinkering point of fiberfill forms difference
The fibrous nodules of shape, obtain filler.
Filament, litchi rind described in step a of the present invention, preferably according to 90-95:5-10 weight ratio, further preferred 95:
5 weight ratio.
High-speed shearing emulsion machine treatment described in step b, preferably time 10-20min, rotating speed is 8000-12000r/
min;Described sieving, preferably crosses 80 mesh sieves.
The present invention can also be one-level spray column built with filler, be water in two grades of spray columns.
Compared with prior art, the present invention has advantages below:
1st, in the prior art, the waste gas for being produced come the production of absorption extraction thing using the spray column of the level Four of series connection, level Four spray
The liquid phase substance drenched in tower is respectively and with the addition of the relatively low alkali lye of concentration of xanthans, with the addition of the concentration of xanthans alkali higher
Liquid, with the addition of the concentration of xanthans alkali lye and water higher, but in being produced for Olive leaf P.E foul waste gas treatment,
Effect is bad.Using the method for the present invention, the stench of a large amount of olive leaves in Olive leaf P.E production process can be effectively absorbed
Waste gas, absorbed using in the 3-4 grade spray column of the alkali lye that with the addition of xanthans compared to existing technology, effect is obvious, and
And, the present invention is utilized in being absorbed in the 1-2 grades of spray column that with the addition of filler, shortens the operation used time, has saved cost.
2nd, the purpose of clean water can be reached, but work as with the various impurity in filter water the characteristics of the fibrous nodules of filtering
When containing substantial amounts of waste gas in water, common fibrous nodules filler can not but play preferably effect, and the present invention is by modified
Fibrous nodules filler, when being contacted with the water containing waste gas, can effectively adsorb the waste gas in water, and, the filler that the present invention is obtained, first
Contacted with hydrone, one layer of diaphragm of water is formed on fibrous nodules filler surface, wrapped waste gas, it is easy to be flush with water
Get off.
2nd, the present invention in fibrous nodules filler by adding the litchi rind of specially treated come modified, the litchi rind to fibrous nodules
In contain substantial amounts of cellulose, cellulose be by glucose group into macromolecular polysaccharide, water insoluble and common organic solvents are
The main component of plant cell wall, but the fiber in litchi rind plant cell is bonded by lignin, it is not easy to break.It is of the invention first
Litchi rind is processed using high pressure microjet superfine communication technique, the fiber of litchi rind can be fully disconnected, then using pressurized treatments,
Steam blasting, under high temperature, high steam effect, cellulose crystallity is improved, and the degree of polymerization declines, hemicellulose fraction degraded,
Lignin softens, and horizontal strength of connection declines, or even softening is plastic, when the material sudden pressure reduction full of steam, in hole
The acute expansion of gas, produce " explosion " effect, lignin can be partially stripped, and be fiber fines by raw material tear.By such place
Reason, can produce package action to emission molecule well using the cellulose in litchi rind.If using 100-1000MPa
Pressure treatment, albumen in plant material, polysaccharose substance structure can be caused to change, so as to reduce the modified effect of fibrous nodules
Really.
Specific embodiment
With embodiment, the invention will be further described below, but the invention is not limited in these embodiments.
Embodiment 1:
The processing method of waste gas, comprises the following steps in a kind of Olive leaf P.E production:
1) spray column absorbs:Enter spray column treatment after in the exhaust gas centralized that will be produced in production;
Spray column is the two-stage of series connection, and built with filler, the liquid phase substance in spray column is water, two grades of sprays to two-stage spray column
Drench tower to shield, and couple with subsequent technique treatment;
2) gas that treatment is completed is by pipeline to factory's inner chimney high altitude discharge;
Described filler is prepared by the following method:
A, raw material prepare:According to 90:10 weight are than preparing filament, litchi rind;
The treatment of b, litchi rind:
1. pulverization process:Crush or the pure water equivalent to litchi rind 8-10 weight is added after smashing, with high speed shear breast
The treatment of change machine, time 10min, rotating speed is 12000r/min, then with high pressure microjet Ultra-Micro Grinding Equipment at 25 DEG C
Reason, processing pressure is 50MPa, and number of processes is 2-3 times, obtains paste serous material;
2. steam blasting:The material that 1. step obtains is put into steam blasting tank, burst pressure 3.0Mpa, dwell time dimension
Hold in 150s;
3. decoct:The pure water of the weights such as the material addition that 2. step is obtained is decocted 2 times, 1 hour every time, is extracted
Liquid, filtering merges extract solution, and the medicinal extract that relative density is 1.30 is surveyed when filtrate is concentrated into 70 DEG C, dries, and crosses 80 mesh sieves, obtains powder
End;
C, by filament bunchy, make fibre bundle clamp stretch;Fibre bundle is spaced fusing with ultrasonic bonding head and forms molten
Node, the litchi rind powder for adding step b to obtain while fusing, is conveyed the good fibre bundle of clinkering by transmission device;Use knife
Piece carries out cutting the fiberfill to form same size, and launching fibre bundle as constraint point with the clinkering point of fiberfill forms difference
The fibrous nodules of shape, obtain filler.
Embodiment 2:
The processing method of waste gas, comprises the following steps in a kind of Olive leaf P.E production:
1) spray column absorbs:Enter spray column treatment after in the exhaust gas centralized that will be produced in production;
Spray column is the two-stage of series connection, and built with filler, the liquid phase substance in spray column is water, two grades of sprays to two-stage spray column
Drench tower to shield, and couple with subsequent technique treatment;
2) gas that treatment is completed is by pipeline to factory's inner chimney high altitude discharge;
Described filler is prepared by the following method:
A, raw material prepare:According to 92:8 weight are than preparing filament, litchi rind;
The treatment of b, litchi rind:
1. pulverization process:Crush or the pure water equivalent to litchi rind 8-10 weight is added after smashing, with high speed shear breast
The treatment of change machine, time 20min, rotating speed is 8000r/min, then with high pressure microjet Ultra-Micro Grinding Equipment at 25 DEG C
Reason, processing pressure is 55MPa, and number of processes is 2-3 times, obtains paste serous material;
2. steam blasting:The material that 1. step obtains is put into steam blasting tank, burst pressure 3.5Mpa, dwell time dimension
Hold in 200s;
3. decoct:The pure water of the weights such as the material addition that 2. step is obtained is decocted 2 times, 1 hour every time, is extracted
Liquid, filtering merges extract solution, and the medicinal extract that relative density is 1.30 is surveyed when filtrate is concentrated into 70 DEG C, dries, and crosses 80 mesh sieves, obtains powder
End;
C, by filament bunchy, make fibre bundle clamp stretch;Fibre bundle is spaced fusing with ultrasonic bonding head and forms molten
Node, the litchi rind powder for adding step b to obtain while fusing, is conveyed the good fibre bundle of clinkering by transmission device;Use knife
Piece carries out cutting the fiberfill to form same size, and launching fibre bundle as constraint point with the clinkering point of fiberfill forms difference
The fibrous nodules of shape, obtain filler.
Embodiment 3:
The processing method of waste gas, comprises the following steps in a kind of Olive leaf P.E production:
1) spray column absorbs:Enter spray column treatment after in the exhaust gas centralized that will be produced in production;
Spray column is the two-stage of series connection, and built with filler, the liquid phase substance in spray column is water, two grades of sprays to two-stage spray column
Drench tower to shield, and couple with subsequent technique treatment;
2) gas that treatment is completed is by pipeline to factory's inner chimney high altitude discharge;
Described filler is prepared by the following method:
A, raw material prepare:According to 95:5 weight are than preparing filament, litchi rind;
The treatment of b, litchi rind:
1. pulverization process:Crush or the pure water equivalent to litchi rind 8-10 weight is added after smashing, with high speed shear breast
The treatment of change machine, time 15min, rotating speed is 10000r/min, then with high pressure microjet Ultra-Micro Grinding Equipment at 25 DEG C
Reason, processing pressure is 60MPa, and number of processes is 2-3 times, obtains paste serous material;
2. steam blasting:The material that 1. step obtains is put into steam blasting tank, burst pressure 3.5Mpa, dwell time dimension
Hold in 180s;
3. decoct:The pure water of the weights such as the material addition that 2. step is obtained is decocted 2 times, 1 hour every time, is extracted
Liquid, filtering merges extract solution, and the medicinal extract that relative density is 1.30 is surveyed when filtrate is concentrated into 70 DEG C, dries, and crosses 80 mesh sieves, obtains powder
End;
C, by filament bunchy, make fibre bundle clamp stretch;Fibre bundle is spaced fusing with ultrasonic bonding head and forms molten
Node, the litchi rind powder for adding step b to obtain while fusing, is conveyed the good fibre bundle of clinkering by transmission device;Use knife
Piece carries out cutting the fiberfill to form same size, and launching fibre bundle as constraint point with the clinkering point of fiberfill forms difference
The fibrous nodules of shape, obtain filler.
Experimental example:
The processing method of waste gas, comprises the following steps in Olive leaf P.E production:
1) spray column absorbs:Enter spray column treatment after in the exhaust gas centralized that will be produced in production;
Spray column is the two-stage of series connection, and built with the filler of embodiment 3, the liquid phase substance in spray column is two-stage spray column
Water, two grades of spray columns shield, and couple with subsequent technique treatment;
2) gas that treatment is completed is by pipeline to factory's inner chimney high altitude discharge.
Comparative example:
1) spray column absorbs:Enter spray column treatment after in the exhaust gas centralized that will be produced in production;
Spray column be series connection level Four, the liquid phase substance in spray column is water, and two grades of spray columns shield, and with it is rear
Continuous PROCESS FOR TREATMENT connection;
2) gas that treatment is completed is by pipeline to factory's inner chimney high altitude discharge;
Spray column be series connection level Four, the liquid phase substance in level Four spray column be respectively with the addition of xanthans concentration it is relatively low
Alkali lye, with the addition of the concentration of xanthans alkali lye higher, with the addition of the concentration of xanthans alkali lye and water higher, concentration is higher
Alkali lye be 2% mass concentration Na2CO3Solution, the relatively low alkali lye of concentration is the Na of 1% mass concentration2CO3Solution, in alkali lye
All with the addition of the xanthans of 0.5% mass concentration.
Conclusion:The result of embodiment 3 is far superior to comparative example.
Claims (5)
1. the processing method of waste gas during a kind of Olive leaf P.E is produced, it is characterised in that comprise the following steps:
1) spray column absorbs:Enter spray column treatment after in the exhaust gas centralized that will be produced in production;
Spray column is the two-stage of series connection, and built with filler, the liquid phase substance in spray column is water, two grades of spray columns to two-stage spray column
Shield, and couple with subsequent technique treatment;
2) gas that treatment is completed is by pipeline to factory's inner chimney high altitude discharge;
Described filler is prepared by the following method:
A, raw material prepare:Prepare filament, litchi rind;
The treatment of b, litchi rind:
1. pulverization process:Crush or the pure water equivalent to litchi rind 8-10 weight is added after smashing, use high-speed shearing emulsion machine
Treatment, is then processed with high pressure microjet Ultra-Micro Grinding Equipment in 25 DEG C, and processing pressure is 50-60MPa, and number of processes is
2-3 times, obtain paste serous material;
2. steam blasting:The material that 1. step obtains is put into steam blasting tank, burst pressure 3.0-3.5Mpa, dwell time dimension
Hold in 150-200s;
3. decoct:The pure water of the weights such as the material addition that 2. step is obtained is decocted 2 times, 1 hour every time, obtains extract solution, mistake
Filter, merges extract solution, and the medicinal extract that relative density is 1.30 is surveyed when filtrate is concentrated into 70 DEG C, dries, and sieving obtains powder;
C, by filament bunchy, make fibre bundle clamp stretch;Fibre bundle is spaced fusing with ultrasonic bonding head and forms clinkering point,
The litchi rind powder for adding step b to obtain while fusing, is conveyed the good fibre bundle of clinkering by transmission device;Carried out with blade
Cutting forms the fiberfill of same size, and launching fibre bundle as constraint point with the clinkering point of fiberfill forms of different shapes
Fibrous nodules, obtain filler.
2. the processing method of waste gas during a kind of Olive leaf P.E according to claim 1 is produced, it is characterised in that:Step
Filament, litchi rind described in a, according to 90-95:5-10 weight ratio.
3. the processing method of waste gas during a kind of Olive leaf P.E according to claim 3 is produced, it is characterised in that:Step
Filament, litchi rind described in a, according to 95:5 weight ratios.
4. the processing method of waste gas during a kind of Olive leaf P.E according to claim 1 is produced, it is characterised in that:Step
High-speed shearing emulsion machine treatment described in b, time 10-20min, rotating speed is 8000-12000r/min.
5. the processing method of waste gas during a kind of Olive leaf P.E according to claim 1 is produced, it is characterised in that:Step
Sieving described in b, to cross 80 mesh sieves.
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080141858A1 (en) * | 2006-12-18 | 2008-06-19 | Chunqing Liu | Gas Separations Using High Performance Mixed Matrix Membranes |
CN104262423A (en) * | 2014-09-30 | 2015-01-07 | 桂林三宝药业有限公司 | Method for extracting phlorhizin from litchi rind |
CN104524946A (en) * | 2014-12-31 | 2015-04-22 | 桂林市世环废气处理设备有限公司 | Waste gas treatment method in production of fragant peony extract |
CN105148609A (en) * | 2015-08-31 | 2015-12-16 | 曾金华 | Hydrophilic and oleophobic filter material and preparation method thereof |
-
2016
- 2016-11-30 CN CN201611079570.XA patent/CN106731492A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080141858A1 (en) * | 2006-12-18 | 2008-06-19 | Chunqing Liu | Gas Separations Using High Performance Mixed Matrix Membranes |
CN104262423A (en) * | 2014-09-30 | 2015-01-07 | 桂林三宝药业有限公司 | Method for extracting phlorhizin from litchi rind |
CN104524946A (en) * | 2014-12-31 | 2015-04-22 | 桂林市世环废气处理设备有限公司 | Waste gas treatment method in production of fragant peony extract |
CN105148609A (en) * | 2015-08-31 | 2015-12-16 | 曾金华 | Hydrophilic and oleophobic filter material and preparation method thereof |
Non-Patent Citations (2)
Title |
---|
王家德 等: "《现代环境生物工程》", 31 May 2014, 化学工业出版社 * |
闫军 等: "蒸汽爆破技术的研究", 《现代农业科技》 * |
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