ITBZ20110030A1 - METHOD FOR THE RECOVERY OF LIQUIDS POLLUTANT WITH WASTE VEGETABLE PRODUCTS COMING FROM INDUSTRIAL PROCESSING, ANIMAL EXPRESSIONS OR HYDROCARBONS. - Google Patents

METHOD FOR THE RECOVERY OF LIQUIDS POLLUTANT WITH WASTE VEGETABLE PRODUCTS COMING FROM INDUSTRIAL PROCESSING, ANIMAL EXPRESSIONS OR HYDROCARBONS. Download PDF

Info

Publication number
ITBZ20110030A1
ITBZ20110030A1 IT000030A ITBZ20110030A ITBZ20110030A1 IT BZ20110030 A1 ITBZ20110030 A1 IT BZ20110030A1 IT 000030 A IT000030 A IT 000030A IT BZ20110030 A ITBZ20110030 A IT BZ20110030A IT BZ20110030 A1 ITBZ20110030 A1 IT BZ20110030A1
Authority
IT
Italy
Prior art keywords
vegetable
product
waste
coming
absorption
Prior art date
Application number
IT000030A
Other languages
Italian (it)
Inventor
Alberto Volcan
Original Assignee
Alberto Volcan
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Alberto Volcan filed Critical Alberto Volcan
Priority to IT000030A priority Critical patent/ITBZ20110030A1/en
Priority to PCT/EP2011/068671 priority patent/WO2012055876A1/en
Publication of ITBZ20110030A1 publication Critical patent/ITBZ20110030A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2220/00Aspects relating to sorbent materials
    • B01J2220/40Aspects relating to the composition of sorbent or filter aid materials
    • B01J2220/48Sorbents characterised by the starting material used for their preparation
    • B01J2220/4875Sorbents characterised by the starting material used for their preparation the starting material being a waste, residue or of undefined composition
    • B01J2220/4887Residues, wastes, e.g. garbage, municipal or industrial sludges, compost, animal manure; fly-ashes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/048Purification of waste water by evaporation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/286Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F2001/5218Crystallization
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/20Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/22Nature of the water, waste water, sewage or sludge to be treated from the processing of animals, e.g. poultry, fish, or parts thereof
    • C02F2103/24Nature of the water, waste water, sewage or sludge to be treated from the processing of animals, e.g. poultry, fish, or parts thereof from tanneries

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

Titolo: Metodo per il recupero di liquidi inquinanti con prodotti vegetali di scarto provenienti da lavorazioni industriali, di escrementi animali o di idrocarburi Title: Method for the recovery of polluting liquids with waste vegetable products from industrial processes, animal excrement or hydrocarbons

La presente invenzione si riferisce a un metodo per il recupero di liquidi inquinanti con prodotti vegetali di scarto provenienti da lavorazioni industriali, di escrementi animali o di idrocarburi secondo la parte classificante della rivendicazione 1. The present invention relates to a method for recovering polluting liquids with waste vegetable products from industrial processes, animal excrements or hydrocarbons according to the classifying part of claim 1.

È noto il problema di poter smaltire le acque luride, acque luride alcaline e acide derivanti da concerie o anche da escrementi liquidi di animali. The problem of being able to dispose of sewage, alkaline and acid sewage deriving from tanneries or even from liquid animal excrements is known.

Lo scopo della presente invenzione à ̈ di realizzare una barriera di materiale vegetale per l’assorbimento di liquidi inquinanti. Questo scopo viene raggiunto da un metodo per il recupero di liquidi inquinanti con prodotti vegetali di scarto provenienti da lavorazioni industriali secondo la parte caratterizzante della rivendicazione 1. The purpose of the present invention is to realize a barrier of plant material for the absorption of polluting liquids. This object is achieved by a method for the recovery of polluting liquids with vegetable waste products coming from industrial processes according to the characterizing part of claim 1.

L’assorbimento di liquidi inquinanti provenienti da concerie, impianti di trattamento acque ed altri prodotti liquidi inquinanti da sali industriali ed altre sostanze chimiche. costituisce una barriera alla discarica di liquidi inquinanti. The absorption of polluting liquids from tanneries, water treatment plants and other liquid products polluting from industrial salts and other chemical substances. it constitutes a barrier to the landfill of polluting liquids.

La barriera di prodotti vegetali à ̈ formata da scarti industriali con dimensioni da 200, 300 fino a 600 micron in base del prodotto solido utilizzato. The vegetable product barrier is formed by industrial waste with dimensions from 200, 300 up to 600 microns based on the solid product used.

Dopo l’utilizzo delle barriere queste possono essere raccolte e spremute e utilizzando il prodotto iniziale (per esempio sale per concerie). After the use of the barriers these can be collected and squeezed and using the initial product (for example salt for tanneries).

Il metodo comprende le seguenti fasi: The method includes the following steps:

Assorbimento per esempio di 15 minuti Absorption for example of 15 minutes

spremitura meccanica mechanical squeezing

cristallizzazione per 12 ore. crystallization for 12 hours.

L’assorbimento del liquido lurido salato proveniente per esempio da concerie scorre condensato all’interno del “fagotto†assorbente di lunghezza e di dimensioni da stabilire in base allo scarico: può essere di forma cilindrica contenente il vegetale e di formata a barriera. Stabilito il tempo di assorbimento se il liquido à ̈ stabile e ca, 15,30’ in base alle dimensioni, sarà maggiore di 30’ se il liquido sarà in movimento. Con il metodo meccanico si spreme il“fagotto†per mezzo di rulli e si deposita in contenitori per l’evaporazione dell’acqua, mentre il rimanente à ̈ il rifiorire del sale per la sua riutilizzazione. Il tempo della cristallizzazione à ̈ determinato dalla temperatura“forzata†o non e dalla quantità del prodotto esposto. The absorption of the salty dirty liquid coming for example from tanneries flows condensed inside the absorbent â € œfagottoâ € of length and size to be established based on the drain: it can be cylindrical in shape containing the vegetable and formed as a barrier . Once the absorption time has been established if the liquid is stable and approximately 15.30â € ™ based on the size, it will be greater than 30â € ™ if the liquid will be in motion. With the mechanical method the â € œfagottoâ € is squeezed by means of rollers and it is deposited in containers for the evaporation of the water, while the remainder is the flourishing of the salt for its reuse. The crystallization time is determined by the â € œforcedâ € or non-forced temperature and the quantity of the product displayed.

Con il metodo con la spremitura meccanica à ̈ preferibile un prodotto vegetale di scarto “grezzo†con granulometria micrometrica da 600/700 micron. Dopo la spremitura uscirà un liquido composto da acqua e sali ed altri inquinanti, pronto per la cristallizzazione , With the mechanical squeezing method, a “raw” vegetable waste product with a micrometric particle size of 600/700 microns is preferable. After squeezing, a liquid composed of water and salts and other pollutants will come out, ready for crystallization,

Un altro metodo efficace consiste nell’aprire del “fagotto†e della “barriera†e depositarlo per la cristallizzazione che avverrà dopo 10/12 ore. Il sale rifiorirà dall’interno del prodotto vegetale sotto forma di cristalli. Con questo metodo il prodotto vegetale proveniente da scarti di mele, scarti di arancia od altri vegetali avrà dimensioni da 200/300 micron. Another effective method consists in opening the â € œfagottoâ € and the â € œbarrierâ € and depositing it for crystallization which will take place after 10/12 hours. The salt will bloom again from the inside of the plant product in the form of crystals. With this method the vegetable product coming from apple scraps, orange scraps or other vegetables will have dimensions of 200/300 microns.

Oltre alla forma di impacco il materiale vegetale potrebbe presentarsi anche sotto forma di materiale cospargibile o polverulenta così da poter stenderlo su inquinanti da assorbire, per esempio escrementi di animali. In questo caso o il materiale assorbito può essere messo in un contenitore insieme con lo scarto di vegetale per sottoporlo ad un opportuno trattamento termico o esso può essere raccolto in un sacchetto per spremerlo. In addition to the form of a compress, the plant material could also be in the form of spreadable or powdery material so that it can be spread on pollutants to be absorbed, for example animal excrement. In this case either the absorbed material can be placed in a container together with the vegetable waste to subject it to an appropriate heat treatment or it can be collected in a bag to squeeze it.

Il metodo può essere riassunto come segue: The method can be summarized as follows:

in una prima fase il prodotto inquinante investe il prodotto vegetale in a first phase the polluting product invests the vegetable product

in una seconda fase il prodotto vegetale assorbe il prodotto inquinante per un lasso di tempo in a second phase the vegetable product absorbs the polluting product for a period of time

in una terza fase il prodotto assorbito viene raccolto insieme con il prodotto assorbente in a third phase the absorbed product is collected together with the absorbent product

in una quarta fase il prodotto raccolto viene spremuto in a fourth phase the collected product is squeezed

in una quinta fase il prodotto spremuto meccanicamente viene lasciato cristallizzare per un periodo di tempo in a fifth phase the mechanically squeezed product is left to crystallize for a period of time

In una forma di realizzazione l’assorbimento ha una durata di 15 minuti In one embodiment, the absorption lasts for 15 minutes

In un’altra forma di realizzazione la durata di cristallizzazione à ̈ di ca.12 ore. In another embodiment, the crystallization time is approx. 12 hours.

In un preferito esempio di realizzazione il prodotto à ̈ impacchettato, l’impacco essendo lasciato investire da un flusso di liquido lurido proveniente da una conceria. In a preferred embodiment, the product is packaged, the pack being left to be invested by a stream of dirty liquid coming from a tannery.

In un altro preferito esempio di realizzazione il materiale vegetale proveniente da scarti industriali viene macinato per ridurlo sotto forma polverulenta da spargere su escrementi animali atti ad essere assorbiti dal materiale vegetale. In another preferred embodiment, the vegetable material coming from industrial waste is ground to reduce it in a powder form to be spread on animal excrements suitable for being absorbed by the vegetable material.

Claims (1)

Rivendicazioni 1. Metodo per il recupero di liquidi inquinanti con prodotti vegetali di scarto provenienti da lavorazioni industriali di escrementi animali liquidi o di idrocarburi caratterizzato dalle seguenti fasi • assorbimento delle sostanze inquinanti contenute nel liquido lurido • spremitura meccanica della sostanza assorbita • cristallizzazione della sostanza spremuta 2. Metodo secondo la rivendicazione 1, caratterizzato dal fatto che l’assorbimento costituisce una barriera di prodotti vegetali formata da scarti industriali con dimensioni da 200, 300 fino a 600 micron in base del prodotto solido utilizzato. 3. Metodo secondo la rivendicazione 1, caratterizzato dal fatto che l’assorbimento ha una durata di 15 minuti 4. Metodo secondo la rivendicazione 1, caratterizzato dal fatto che la cristallizzazione ha una durata di dodici ore. 5. Metodo secondo la rivendicazione 1, caratterizzato dal fatto che il prodotto vegetale à ̈ impacchettato, l’impacco essendo lasciato investire da un flusso di liquido lurido proveniente da una conceria. 6. Metodo secondo la rivendicazione 5, caratterizzato dal fatto che il prodotto vegetale proveniente da scarti di mele, scarti di arancia od altri vegetali avrà dimensioni da 200/300 micron. 7. Metodo secondo la rivendicazione 5, caratterizzato dal fatto che l’impacco ha una forma cilindrica contenente il vegetale e di formata a barriera 8. Metodo secondo la rivendicazione 1, caratterizzato dal fatto il materiale vegetale proveniente da scarti industriali viene macinato per ridurlo sotto forma polverulenta da spargere su escrementi animali atti ad essere assorbiti dal materiale vegetale. 9. Metodo secondo la rivendicazione 1, caratterizzato dal fatto che per la spremitura meccanica à ̈ preferibile un prodotto vegetale di scarto“grezzo†con granulometria micrometrica da 600/700 micron. 10.Prodotto ottenuto secondo una delle rivendicazioni precedenti.Claims 1. Method for the recovery of polluting liquids with waste vegetable products from industrial processing of liquid animal excrements or hydrocarbons characterized by the following phases â € ¢ Absorption of pollutants contained in the dirty liquid â € ¢ mechanical squeezing of the absorbed substance â € ¢ crystallization of the squeezed substance 2. Method according to claim 1, characterized in that the absorption constitutes a barrier of vegetable products formed by industrial waste with dimensions from 200, 300 up to 600 microns based on the solid product used. 3. Method according to claim 1, characterized in that the absorption has a duration of 15 minutes 4. Method according to claim 1, characterized in that the crystallization lasts for twelve hours. 5. Method according to claim 1, characterized in that the vegetable product is packaged, the pack being left to be invested by a stream of dirty liquid coming from a tannery. 6. Method according to claim 5, characterized in that the vegetable product coming from apple scraps, orange scraps or other vegetables will have dimensions of 200/300 microns. 7. Method according to claim 5, characterized in that the pack has a cylindrical shape containing the vegetable and is formed as a barrier 8. Method according to claim 1, characterized in that the plant material coming from industrial waste is ground to reduce it in a powder form to be spread on animal excrements suitable for being absorbed by the plant material. 9. Method according to claim 1, characterized in that for the mechanical pressing it is preferable a vegetable waste product "raw" with a micrometric particle size of 600/700 microns. 10. Product obtained according to one of the preceding claims.
IT000030A 2010-10-25 2011-06-07 METHOD FOR THE RECOVERY OF LIQUIDS POLLUTANT WITH WASTE VEGETABLE PRODUCTS COMING FROM INDUSTRIAL PROCESSING, ANIMAL EXPRESSIONS OR HYDROCARBONS. ITBZ20110030A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
IT000030A ITBZ20110030A1 (en) 2011-06-07 2011-06-07 METHOD FOR THE RECOVERY OF LIQUIDS POLLUTANT WITH WASTE VEGETABLE PRODUCTS COMING FROM INDUSTRIAL PROCESSING, ANIMAL EXPRESSIONS OR HYDROCARBONS.
PCT/EP2011/068671 WO2012055876A1 (en) 2010-10-25 2011-10-25 Material composed of plant products, in particular plant waste products originating from industrial processing, and process for taking up dirt from a liquid or from gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT000030A ITBZ20110030A1 (en) 2011-06-07 2011-06-07 METHOD FOR THE RECOVERY OF LIQUIDS POLLUTANT WITH WASTE VEGETABLE PRODUCTS COMING FROM INDUSTRIAL PROCESSING, ANIMAL EXPRESSIONS OR HYDROCARBONS.

Publications (1)

Publication Number Publication Date
ITBZ20110030A1 true ITBZ20110030A1 (en) 2012-12-08

Family

ID=44554902

Family Applications (1)

Application Number Title Priority Date Filing Date
IT000030A ITBZ20110030A1 (en) 2010-10-25 2011-06-07 METHOD FOR THE RECOVERY OF LIQUIDS POLLUTANT WITH WASTE VEGETABLE PRODUCTS COMING FROM INDUSTRIAL PROCESSING, ANIMAL EXPRESSIONS OR HYDROCARBONS.

Country Status (1)

Country Link
IT (1) ITBZ20110030A1 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4009886A1 (en) * 1990-03-28 1991-10-02 Rheinische Braunkohlenw Ag METHOD FOR TREATING GUELLE
US5122233A (en) * 1989-04-24 1992-06-16 Charles Zampieri Apparatus for the treatment of mixture of brines and contaminated mineral salts
JP2003088900A (en) * 2001-09-19 2003-03-25 Seihachiro Miura Animal excrement treatment method
CN101045564A (en) * 2007-03-26 2007-10-03 浙江大学 Preparation and using method of natural adsorbent for treating organic pollutant water

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5122233A (en) * 1989-04-24 1992-06-16 Charles Zampieri Apparatus for the treatment of mixture of brines and contaminated mineral salts
DE4009886A1 (en) * 1990-03-28 1991-10-02 Rheinische Braunkohlenw Ag METHOD FOR TREATING GUELLE
JP2003088900A (en) * 2001-09-19 2003-03-25 Seihachiro Miura Animal excrement treatment method
CN101045564A (en) * 2007-03-26 2007-10-03 浙江大学 Preparation and using method of natural adsorbent for treating organic pollutant water

Similar Documents

Publication Publication Date Title
Mahmoud Kinetics and thermodynamics of aluminum oxide nanopowder as adsorbent for Fe (III) from aqueous solution
SenthilKumar et al. Removal of copper (II) ions from aqueous solution by adsorption using cashew nut shell
Lavecchia et al. Removal of lead from aqueous solutions by spent tea leaves
Naidu et al. Valuable rubidium extraction from potassium reduced seawater brine
Mishra et al. Removal of endosulfan by sal wood charcoal
Acquah et al. Synthesis and performance analysis of oil palm ash (OPA) based adsorbent as a palm oil bleaching material
Yang et al. Removal of As (III) and As (V) using iron-rich sludge produced from coal mine drainage treatment plant
Oguz Equilibrium isotherms and kinetics studies for the sorption of fluoride on light weight concrete materials
FR2936725B1 (en) PROCESS FOR THE PREPARATION OF A STRUCTURED POROUS MATERIAL COMPRISING METAL PARTICLES 0 INCORPORATED IN THE WALLS.
ITBZ20110030A1 (en) METHOD FOR THE RECOVERY OF LIQUIDS POLLUTANT WITH WASTE VEGETABLE PRODUCTS COMING FROM INDUSTRIAL PROCESSING, ANIMAL EXPRESSIONS OR HYDROCARBONS.
Majeed et al. Adsorption of diclofenac sodium and ibuprofen by bentonite polyureaformaldehyde thermodynamics and kinetics study
Gaur et al. Metal-carbonate formation from ammonia solution by addition of metal salts—An effective method for CO2 capture from landfill gas (LFG)
Jangde et al. Fixed-bed column dynamics of xanthate-modified apple pomace for removal of Pb (II)
CN102309893A (en) Filtering medium for removing PPCPs (pharmaceuticals and personal care products) in drinking water and preparation method thereof
Singh et al. Removal of copper ion from synthetic wastewater using Aloe vera as an adsorbent
Norouzi et al. Essential oil component in leaf and flower of Lemon balm (Melissa officinalis L.)
Kumar et al. Utilization of Erythrina variegata orientalis leaf powder for the removal of cadmium
CN100488889C (en) Sea water desalination later purification filtering method
Gill et al. Extraction of lead through supported liquid membrane using triethanolamine/cyclohexanone carrier and Na2SO4 strippant
Al-Senani et al. Synthesis of PS/RB-Cs and its use in the treatment of water polluted with heavy metals
CN101792383B (en) Method for extracting low concentration perfluorooctanoic acid from fatty substances
Singh et al. Kinetics, thermodynamic and equilibrium study of Cr (VI) adsorption from aqueous solutions by NCL coal dust
Patescu et al. Simultaneous Removal of Lead (II), Nickel (II), Zinc (II) and Copper (II) from Aqueous Solutions by Nano-hydroxyapatite Synthesized by Microwave Field
Lzaod et al. A completely environmentally-friendly methodology for removal of permanent hardness of water using natural materials.
Sulaiman Adsorption of Pb (II), Zn (II) and Fe (II) using Rubber Seed Shell