CN105665422A - Method for recycling stevioside waste residues or filter mud - Google Patents
Method for recycling stevioside waste residues or filter mud Download PDFInfo
- Publication number
- CN105665422A CN105665422A CN201610120581.1A CN201610120581A CN105665422A CN 105665422 A CN105665422 A CN 105665422A CN 201610120581 A CN201610120581 A CN 201610120581A CN 105665422 A CN105665422 A CN 105665422A
- Authority
- CN
- China
- Prior art keywords
- stevioside
- filter mud
- waste residue
- conveyer belt
- fuel
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 49
- UEDUENGHJMELGK-HYDKPPNVSA-N Stevioside Chemical compound O([C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@]12C(=C)C[C@@]3(C1)CC[C@@H]1[C@@](C)(CCC[C@]1([C@@H]3CC2)C)C(=O)O[C@H]1[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O1)O)[C@@H]1O[C@H](CO)[C@@H](O)[C@H](O)[C@H]1O UEDUENGHJMELGK-HYDKPPNVSA-N 0.000 title claims abstract description 38
- 229940013618 stevioside Drugs 0.000 title claims abstract description 38
- OHHNJQXIOPOJSC-UHFFFAOYSA-N stevioside Natural products CC1(CCCC2(C)C3(C)CCC4(CC3(CCC12C)CC4=C)OC5OC(CO)C(O)C(O)C5OC6OC(CO)C(O)C(O)C6O)C(=O)OC7OC(CO)C(O)C(O)C7O OHHNJQXIOPOJSC-UHFFFAOYSA-N 0.000 title claims abstract description 38
- 235000019202 steviosides Nutrition 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract description 14
- 238000004064 recycling Methods 0.000 title abstract description 6
- 239000000446 fuel Substances 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000001035 drying Methods 0.000 claims abstract description 17
- 239000000463 material Substances 0.000 claims abstract description 16
- 239000002028 Biomass Substances 0.000 claims abstract description 8
- 238000007599 discharging Methods 0.000 claims abstract description 6
- 238000001125 extrusion Methods 0.000 claims description 6
- 239000003674 animal food additive Substances 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 229920001202 Inulin Polymers 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 2
- 229930182470 glycoside Natural products 0.000 description 2
- 229940029339 inulin Drugs 0.000 description 2
- -1 inulin glycosides Chemical class 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 241000283690 Bos taurus Species 0.000 description 1
- 241000282887 Suidae Species 0.000 description 1
- 235000001014 amino acid Nutrition 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000021096 natural sweeteners Nutrition 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010563 solid-state fermentation Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B2101/00—Type of solid waste
- B09B2101/02—Gases or liquids enclosed in discarded articles, e.g. aerosol cans or cooling systems of refrigerators
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
- Fodder In General (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention relates to the field of agricultural living thing recycling, and provides a method for recycling stevioside waste residues or filter mud. The method is characterized in that a traditional screw mechanical squeezing manner is changed, at least 30%-45% of water in the waste residues is squeezed out and drained through three-time opposite squeezing modules, and therefore the time and cost for material drying are greatly reduced; and meanwhile, a grinding disk type squeezing structure is adopted, automatic feeding, triple squeezing and discharging are achieved in the whole process, the problem about dewatering of a large amount of matter waste in factories is greatly solved, and the great biotechnology content and the environment-friendly effect are achieved. In addition, the same material, namely, the stevioside waste residues or filter mud, is adopted as a material to be dried and fuel, the comprehensive utilization rate of the waste residues is maximized, and energy is saved synchronously. Even though the material falls into a fuel conveying belt from a conveying belt, no difference is made, the water content of the dried stevioside waste residues is 15% or below, and the stevioside waste residues can be directly sold as finished biomass fodder and fuel.
Description
Technical field
The present invention relates to agro-ecology and recycle field, particularly relate to the recycling of stevioside waste residue and filter mud.
Background technology
Leaf of Folium Stevlae Rebaudianae is containing inulin glycosides 6-12%, and fine work is white powder, is the natural sweetener of a kind of low in calories, high sugariness, is one of the raw material of food and pharmaceutical industries. Refine in the course of processing producing, can produce substantial amounts of waste residue and filter mud, and possibly together with inulin glycosides in this part waste residue and filter mud, waste residue can also be recycled as feedstuff and biomass fuel simultaneously. Current Ge great Folium Stevlae Rebaudianae processing enterprise is all less desirable for the process of waste residue and filter mud, and the stacking of filter mud stores and brings pollution hidden trouble more to make us load to disturb.
Stevioside Solid state fermentation high-quality biomass out, it is possible to as domestic animals such as feed supply pigs and cattle, experiments show that, the protein content of this kind of feedstuff is more than 35%, possibly together with necessary nutrient substance of animal such as substantial amounts of aminoacid, crude fibres. Due in stevioside waste residue containing the water yield up to 65%, bring great difficulty to recycling.
Common squeezing process method cannot by the moisture Control in waste residue below 30%, and this just brings very big cost to drying, and meanwhile, moisture does not control cannot burn below 35% yet, and namely drying to increase electric energy or fuel cost. And this cost like this needs to lean on the product that low profit walks amount cannot adapt to the market competition at feedstuff and fuel, it is easy to be eliminated. Therefore, the recycling how improving stevioside waste residue is worth just more urgent.
Summary of the invention
The purpose of the present invention is aiming at above technical problem, it is provided that a kind of stevioside waste residue filter mud recoverying and utilizing method, and stevioside waste residue filter mud is made biomass feed and fuel.
The technical problem of the present invention is addressed mainly through following technical proposals:
A kind of stevioside waste residue filter mud recoverying and utilizing method, it is characterised in that step is as follows:
A. adopting conveyer belt to send into press dewatering equipment feed hopper the water content stevioside waste residue filter mud up to 60～70%, described conveyer belt is arranged over magnetic magnet and removes band ferra thing;
B. described press dewatering equipment is a mill shape, the annular rotary table that it includes a fixed disc and disk is provided with, described rotating disk is uniformly divided into three operation intervals and is synchronously performed, and each operation interval all includes charging, extruding, secondary extrusion, three extruding, five operational modules of discharging are synchronously performed;
C. by obtaining the water content stevioside waste residue filter mud lower than 35% after squeezing, enter back into disintegrating machine and thorough for waste residue briquetting is crushed;
D. the stevioside waste residue filter mud after crushing sends into continuous type drying stove charging aperture through conveyer belt, dries to water content less than 15%;
E. being arranged over material conveyer belt in described its body of heater of continuous type drying stove, be connected with fuel conveyer belt, material conveyer belt, fuel conveyer belt are provided with common charging aperture, not only stevioside waste residue filter mud does fuel but also exist as recovered material;
F. its waste residue of the stevioside after drying can preparing granular or directly pack refined biometric matter feedstuff or pulverize after as feed additive; Its filter mud of stevioside or system 10～20mm is granular or 15*40mm strip processed obtains biomass fuel after drying.
The invention has the beneficial effects as follows: change traditional screw machine extruding and drum extrusion pattern, by three times, formula is extruded module, the moisture in waste residue is extruded and discharges at least 30～45%, thus greatly reducing time and the cost of drying materials; Meanwhile, adopt abrasive disk type extrusion structure, whole-process automatic charging, triple extruding, discharging, solve the dehydration problem of a large amount of matter waste of factory greatly, possess great biotechnology content and have environmental protection effect. Additionally, material to be dried and fuel adopt commaterial, it is all stevioside waste residue or filter mud, makes waste residue comprehensive utilization ratio realize maximizing, the synchronous saving energy. Even if material falls on fuel conveyer belt also unimportant from conveyer belt, the stevioside waste residue water content after drying is less than 15%, can directly sell as biomass feed and fuel finished product.
Accompanying drawing explanation
Fig. 1 is the press dewatering device structure schematic diagram in the present invention.
In figure: 1. disk; 2. rotating disk; 3. charging; 4. once extrude; 5. secondary extrusion; 6. three extruding; 7. discharging.
Detailed description of the invention
By the examples below, and in conjunction with accompanying drawing, technical scheme is described in further detail.
Embodiment 1:
A kind of stevioside waste residue filter mud recoverying and utilizing method, step is as follows:
A. adopting conveyer belt to send into press dewatering equipment feed hopper the water content stevioside waste residue filter mud up to 60～70%, described conveyer belt is arranged over magnetic magnet and removes band ferra thing; Waste residue and filter mud ratio 7:3, add up to 15kg, water content 65%.
B. described press dewatering equipment is a mill shape, diameter 3m, the annular rotary table 2 that it includes a fixed disc 1 and disk 1 is provided with, described rotating disk 2 is uniformly divided into three operation intervals and is synchronously performed, and each operation interval all includes charging 3, once extrudes 4, secondary extrusion 5, three extruding 6,7 five operational modules of discharging are synchronously performed; Each hopper can fill 15kg stevioside waste residue filter mud, 6.056kg after press dewatering, water content 31.66%.
C. by obtaining the water content stevioside waste residue filter mud lower than 35% after squeezing, enter back into disintegrating machine and thorough for waste residue briquetting is crushed;
D. the stevioside waste residue filter mud after crushing sends into continuous type drying stove charging aperture through conveyer belt, dries to water content less than 15%;
E. being arranged over material conveyer belt in described its body of heater of continuous type drying stove, be connected with fuel conveyer belt, material conveyer belt, fuel conveyer belt are provided with common charging aperture, not only stevioside waste residue filter mud does fuel but also exist as recovered material;
F. its waste residue of the stevioside after drying can preparing granular or directly pack refined biometric matter feedstuff or pulverize after as feed additive; Its filter mud of stevioside or system 10～20mm is granular or 15*40mm strip processed obtains biomass fuel after drying.
Embodiment 2:
It is different in that with embodiment 1, stevioside waste residue and filter mud ratio 1:1, water content 65%. Water content 33.29% after press dewatering.
Embodiment 3:
Being different in that with embodiment 1, raw material is only with stevioside waste residue, water content 65%. Water content 28.9% after press dewatering.
The present embodiment is the embodiment of example of the present invention; for those skilled in the art; the invention discloses on the basis of application process and principle; it is easy to make various types of improvement or deformation; being not limited solely to the structure described by the above-mentioned detailed description of the invention of the present invention, therefore previously described mode is preferred version, and does not have restrictive meaning; every equivalence made according to the present invention changes and amendment, all in the scope protection domain of claims of the present invention.
Claims (1)
1. a stevioside waste residue filter mud recoverying and utilizing method, it is characterised in that step is as follows:
A. adopting conveyer belt to send into press dewatering equipment feed hopper the water content stevioside waste residue filter mud up to 60～70%, described conveyer belt is arranged over magnetic magnet and removes band ferra thing;
B. described press dewatering equipment is a mill shape, the annular rotary table that it includes a fixed disc and disk is provided with, described rotating disk is uniformly divided into three operation intervals and is synchronously performed, and each operation interval all includes charging, extruding, secondary extrusion, three extruding, five operational modules of discharging;
C. by obtaining the water content stevioside waste residue filter mud lower than 35% after squeezing, enter back into disintegrating machine and thorough for waste residue briquetting is crushed;
D. the stevioside waste residue filter mud after crushing sends into continuous type drying stove charging aperture through conveyer belt, dries to water content less than 15%;
E. being arranged over material conveyer belt in described its body of heater of continuous type drying stove, be connected with fuel conveyer belt, material conveyer belt, fuel conveyer belt are provided with common charging aperture, not only stevioside waste residue filter mud does fuel but also exist as recovered material;
F. its waste residue of the stevioside after drying can preparing granular or directly pack refined biometric matter feedstuff or pulverize after as feed additive; Its filter mud of stevioside or system 10～20mm is granular or 15*40mm strip processed obtains biomass fuel after drying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610120581.1A CN105665422B (en) | 2016-03-03 | 2016-03-03 | A kind of stevioside waste residue filter mud recoverying and utilizing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610120581.1A CN105665422B (en) | 2016-03-03 | 2016-03-03 | A kind of stevioside waste residue filter mud recoverying and utilizing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105665422A true CN105665422A (en) | 2016-06-15 |
| CN105665422B CN105665422B (en) | 2018-08-17 |
Family
ID=56306623
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610120581.1A Expired - Fee Related CN105665422B (en) | 2016-03-03 | 2016-03-03 | A kind of stevioside waste residue filter mud recoverying and utilizing method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105665422B (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1511466A (en) * | 2002-12-27 | 2004-07-14 | 上海神灵煤气设备工程有限公司 | Process for preparing regenerated fodder from kitchen wastes |
| CN1810928A (en) * | 2006-03-07 | 2006-08-02 | 李峰耀 | Comprehensive biomass solidifying, carbonizing and gasifying utilization process |
| CN101497836A (en) * | 2008-01-29 | 2009-08-05 | 雷菊花 | Organic waste solid moulding fuel and production method thereof |
| CN101892108A (en) * | 2010-08-19 | 2010-11-24 | 福建泰和木业有限公司 | Production process of environmental-protection plant energy particle fuel |
| CN101979477A (en) * | 2010-09-17 | 2011-02-23 | 常小勇 | Biomass moulding fuel rod and process for producing same |
| JP2011083654A (en) * | 2009-10-13 | 2011-04-28 | Ugajin Seisakusho:Kk | Organic waste treatment apparatus and method of producing fertilizer and solid fuel containing organic waste as component using the apparatus |
| WO2012029182A1 (en) * | 2010-09-03 | 2012-03-08 | 三菱重工業株式会社 | Apparatus and method for biomass decomposition, and system for producing sugar solution using biomass raw material |
| CN102625826A (en) * | 2009-09-04 | 2012-08-01 | 迪芬巴赫机械工程有限公司 | Method and system for producing pellets from biomass in a pellet press for use as fuel in fireplaces |
-
2016
- 2016-03-03 CN CN201610120581.1A patent/CN105665422B/en not_active Expired - Fee Related
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1511466A (en) * | 2002-12-27 | 2004-07-14 | 上海神灵煤气设备工程有限公司 | Process for preparing regenerated fodder from kitchen wastes |
| CN1810928A (en) * | 2006-03-07 | 2006-08-02 | 李峰耀 | Comprehensive biomass solidifying, carbonizing and gasifying utilization process |
| CN101497836A (en) * | 2008-01-29 | 2009-08-05 | 雷菊花 | Organic waste solid moulding fuel and production method thereof |
| CN102625826A (en) * | 2009-09-04 | 2012-08-01 | 迪芬巴赫机械工程有限公司 | Method and system for producing pellets from biomass in a pellet press for use as fuel in fireplaces |
| JP2011083654A (en) * | 2009-10-13 | 2011-04-28 | Ugajin Seisakusho:Kk | Organic waste treatment apparatus and method of producing fertilizer and solid fuel containing organic waste as component using the apparatus |
| CN101892108A (en) * | 2010-08-19 | 2010-11-24 | 福建泰和木业有限公司 | Production process of environmental-protection plant energy particle fuel |
| WO2012029182A1 (en) * | 2010-09-03 | 2012-03-08 | 三菱重工業株式会社 | Apparatus and method for biomass decomposition, and system for producing sugar solution using biomass raw material |
| CN101979477A (en) * | 2010-09-17 | 2011-02-23 | 常小勇 | Biomass moulding fuel rod and process for producing same |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105665422B (en) | 2018-08-17 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: He Guanting Inventor before: He Guohua |
|
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20180122 Address after: 341000 Jiangxi city of Ganzhou province Zhanggong district under Hao Tang No. 1 building 602 room 4 Applicant after: He Guanting Address before: 341000 Jiangxi city of Ganzhou province Zhanggong district under Hao Tang No. 1 building 602 room 4 Applicant before: He Guohua |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180817 |