TOMSA DESTIL ® is a Spanish company specialized in the engineering and
manufacturing of alcohol distillation plants and related products in the
international market. Equipped with highly experienced personnel, TOMSA is
reputed for having substantially improved the processes for producing alcohol,
with a view to obtaining the best possible product at the lowest operating cost.
TOMSA´s engineering capabilities are coupled with its ability to design and
build equipment for each and every specific production area of the distillation
process. TOMSA DESTIL ® is a "Turn-key" engineering and manufacturing
company for every single aspect of the alcohol distillation process.
In the early 1970´s, TOMSA DESTIL ® was one of the pioneers in the
development and commissioning of the vacuum distillation system
(Multipressure system.) As a result of this, TOMSA rapidly expanded in the
international market, building distilleries in all five continents of the world,
gaining experience with all types of raw materials.
In the production of all the different types of alcohols (fuel alcohol, industrial
alcohol and potable alcohol), TOMSA DESTIL ® offers its know-how, to
producers of each and every aspect of the alcohol manufacturing process and
associated services and utilities. TOMSA´s equipment and process designs uses
the latest "state of the art" methods adapted to suite each customers particular
requirements in such a way that enables TOMSA to be a flexible supplier to all
of its individual customers.
ACTIVITIES
¾ Storage and Handling of Raw Feeds
¾ Mash Preparation for:
Molasses
Starch Products (maize, potatoes, agave, etc.)
Fruits (grapes, cherries, apples, etc.)
¾ Continuous or Incremental Fermentation
¾ Atmospheric or vacuum distillation to obtain:
Super fine alcohol
Spirits
Dehydrated Alcohol
¾ Acetic Acid, biochemical or catalic
¾ Treatment of Wastewaters and By-products
¾ Evaporators, Driers, Decanters and Reactors
¾ Molecular sieves for the dehydration of alcohol
¾ Extractive distillation, distillation of essential oils
¾ Distributed Digital Control; Adaptive- Predictive Control
WHAT CAN WE
OFFER?
The latest technology in Fermentation
Distillation
In house Engineering and construction
Operating Know-how of distilleries
Free technical assistance for 5 years (*)
From consultant service to…
Iso-9001 Quality controls
ALSO
Market Studies
Training and Teaching
R+D service for customers
Private laboratories for investigation
Periodical technical reports
(*) Engineers and technicians fees
and
THE ALCOHOL DISTILLERY
The production of alcohol using the different types of raw feeds generally
includes five stages, each one is composed of a group of equipments or
units which are named "Section".
S-200.- Discharge and Storage of the raw feed.
S-300.- Mash preparation
S-400.- Fermentation
S-500.- Distillation
S-600.- Storage of Finished Products
In addition, the Distillery requires a minimum of General Services which
provide the utilities needed:
Civil works and buildings, steam generation, fuel storage, acquisition
and treatment of water, production of compressed air, waste water
treatment,
electrical
installation
and
lighting,
quality
control
laboratories, maintenance workshop and fire protection installation.
TOMSA DESTIL can provide the preliminary study, the engineering
project, the construction or supply completely these Sections and
General Services required by a Distillery.
TYPICAL DISTILLATION COLUMN
A typical distillation column must be equipped with the necessary auxiliary equipment and
instrumentation for its correct operation and control:
1.-Adequate design of the internal components with special dedication to the hydraulic design of
plates and their mass transfer efficiencies.
2.-Correct selection and design of the heating system for the column (reboiler, direct steam, etc.)
and the condensation section for the head vapours.
3.-Automatic control and regulation system, with the optimum selection of the instrumentation type
required, location of the most sensitive zones to minimize perturbations of the system and the
most adequate control logic for the process.
MOLASSES MASH PREPARATION
PROCESS "HYMOL"
Every fermentation process requires previously a preparation of the substrate to be fermented as
well as adjustments to the state of the raw material to adapt to the requirements of the cellular
metabolism of the yeast.
The "HYMOL" process designed by TOMSA for the case of molasses, starts with a precise control
of the feed rate of the incoming molasses and its pre-dilution with water (flows 1 and 10) in
continuous static mixer "MX 313". It is preheated in a counter current flow heat exchanger "E-350"
using the pasteurized mash. Afterwards this mash is pasteurized to 95ºC using direct steam
injection in "E-310". After filtration, addition of nutrients and correction of pH, it is cooled off and
diluted to the required concentrations for the aerobic fermentation, (flow 9) and anaerobic, (flow 7).
The process is continuous and is completely automated.
STARCH MASH PREPARATION
"HYMIDO" PROCESS
An extensive variety of amylaceous cultures as raw material for the alcohol production can be used (maize,
potato, tapioca, etc.) The local climatology, the quality of the soil, the crop resistance and the ease in handling
are, in addition to the starch content, the important criteria when selecting the raw feed to be used.
TOMSA DESTIL offers a continuous hydrolysis and saccarification process using a Jet-cooker based on
consuming the minimum amount steam due to the use of high substrate concentrations and optimizing the
usage and transfer of heat at the different stages of heating and cooling the mash. At the same time, the
productivity of the fermentation is improved substantially as a result of maximising the pre-saccarification of the
starch before going into the fermentation vats.
First, the raw material has to be suitably cleaned. All foreign and non desirable objects which could seriously
damage the equipment must be removed, such as sand, metal objects, etc... Afterwards, the starch is mixed
with hot water and undergoes a partial hydration. This "gelatinisation" produces a viscous mash which must be
treated with thermally stable alpha-amylase enzymes to transform the starch into dextrins. This process, called
"liquefaction" reduces the viscosity of mash and avoids the precipitation of the starch or formation of gels in the
subsequent stages of the process when the temperatures are reduced.
Actually the gelatinisation and the liquefaction occur practically at the same time, and are collectively called
"cooking"
Finally, before fermenting the sacharification of the dextrins with glucose-amylase enzymes is performed at an
average temperature of 60º before finally cooling the mash down in order to go on to the fermentation.
TOMSA DESTIL performs in its laboratories, a case by case study into the specific requirements of each
distillery, determining the expected yields for each type of raw material the client may use.
10
FERMENTATION
The processes of alcoholic fermentation can be classified into two groups: continuous or discontinuous,
and within each group there are two different types of processes depending on whether the process of
yeast production is with a "mother vat" or with "yeast recycling" (the Melle Boinot process and others).
TOMSA DESTIL has developed the technology for all these processes obtaining the highest
transformation yields of alcohol from sugar. This is in a large part due to the techniques of the TOMSA
microbiological laboratories in selecting and improving the “saccaromice cerevisae” yeast strain.
PROCESS USING A MOTHER VAT: "PRO-YEAST"
This consists of continuously generating yeast, from a low concentration mash. The yeast which will be
used later for the alcoholic fermentation is not recovered or recycled.
Mother vats are continuously fed with air (aerobic fermentation). The fermented solution produced will be
composed of a biomass rich in yeast which will be sent to the fermentation vats under the name of "yeast
foot".
The fermentation vats of volumes, greater than the mother vats, are exempt of air (anaerobic fermentation)
and they are fed with a high concentration mash after the yeast foot has been added. If the chosen
process is discontinuous, there will be several fermentation vats, operating intermittently in accordance to
the classic sequence: addition of yeast foot, filling, termination, followed by distillation.
On the contrary, if the process selected is continuous, there will be one or more vats in series in a cascade
fashion, such that the first one continuously receives a flow of yeast foot and mash and the last vat will
have completely fermented mash continuously leaving for the distillery.
In all the cases the fermentation process produces heat (exothermic reaction) and for this reason there
must always be a cooling system for the vats.
PROCESS WITH YEAST RECYCLING: "HY-YEAST"
In this case the yeast foot is substituted by the yeast cream obtained from passing the fermented mash
through a centrifuge separator before distilling it. Depending on each specific case, this yeast cream could
undergo a revitalisation treatment before returning to the fermentation vats.
In this case the yeast foot produced, usually has a smaller volume than that when using the mother vat
process. However it is far richer in yeast biomass.
2
In all the cases the fermentation produces a substantial volume of CO , of a food grade quality that can be
recovered for liquefaction and sale.
PROCESS WITH STILLAGE RECYCLING: "STILL-YEAST"
This process allows fermenting sweetened mash reusing part of the stillage from the distillation section
including all its solid content. This is to replace part of the dilution water and has three fundamental aims: a)
To substantially reduce the volume of spent waste which the distillery has to treat (a smaller net volume of
stillage); b) to reduce the bacterial infections due to the bacteriostatic effect of the high solid concentration
on the fermenting mash; c) to reduce the consumption of nutrients and acid, required by the yeast for
growth and pH balance. Achieved because of the unused salts and acidity contained within the stillage.
It is obvious that this new process requires a yeast strain different from the standard Saccaromices
Cerevisae which has to be able to reproduce themselves within a medium which has a high osmotic
pressure exerted on the cellular membranes.
TOMSA DESTIL has located several wild yeasts able to resist these adverse conditions having modified
and selected this specie for its perfect adaptation to different culture mediums.
" PROVAC PROCESS " (one or two columns)
Based on many years of experience and many distilleries in operation, TOMSA can provide the "PROVAC"
process, as the most efficient method for producing crude alcohol with respect to low energy consumption
and simplicity of operation. One of the greatest advantages of our vacuum distillation systems using
fermented mash, is the complete elimination of scaling and solids settling on the elements inside the
distillation columns.
The combination of our valve design and the special system of downcomer tubes within the column interior
allows it to operate with liquids containing high quantities of suspended solids (grape lees, molasses,
cereals, etc.) without suffering from choking columns, as well as withstanding mash with high scaling
properties or with high concentrations of carbonates and sulphates.
"HYDROVAC" PROCESS (three columns)
When we want to obtain rectified superfine alcohol from raw or impure alcohols such as heads
and tails of previous distillations, the process "HYDROVAC" offers several advantages. It requires
a minimum consumption of energy due to the use of a multi column system operating at differing
pressures in order to obtain a cascade distillation. The system is able to produce alcohol of the
highest quality (organoleptic characteristics and purity) because of the advanced TOMSA
technology in the process of elimination of impurities, heads and hybrid impurities using a
hydroselection column and methanol separation in a demethylizer column. Obtaining in both
cases extractions with high impurity concentrations and so producing minimum volumes of
technical alcohol extracted as by-product.
.
"STILLVAC" SYSTEM (two columns)
With the STILLVAC system TOMSA provides the best technological solution for producing rectified alcohol of
high degree (upto 96.5 ºGL) from fermented mash within the typical quality parameters for the production of
bioethanol or beverage alcohols for maturing (rum, whiskey, brandy, tequila)
The process makes use of all the advantages of "PROVAC" system in terms of vacuum distillation for
fermented mash, since the mash column operates under a vacuum. In addition there is an extra energy saving
that is achieved by having the rectifying column operate under pressure which enables the two columns to work
as a dual effect using the vapours from the head of the rectifier (high temperature) to heat up the base of the
mash column (low temperature) without additional energy consumption required by this latter column. This heat
transfer is achieved using a falling film reboiler. The whole process is commonly referred to the "multipressure
column system"
The volatile impurities (heads) contained in fermented mash are eliminated from the zones at the head of each
of the column and the heavy impurities (tails) are eliminated both from the bottom of the mash column and from
the central zone of the rectifying column. Depending on the type of raw feed used, the mash column reboiler will
operate using stillage recirculation to produce the steam for the column or with spent lees (distilled water)
obtained from the foot of the rectifying column, if there is a danger of scaling in the reboiler tubes.
.
SUPERFINE ALCOHOL FROM FERMENTED MASH
"FINEVAC" PROCESS
This is the combination of the PROVAC and the HYDROVAC processes properly readjusted to permit the
production of mainly superfine alcohol from fermented mash using the minimum consumption of energy
and the highest quality of rectified alcohol as required by the international liquor and cosmetics industries.
ANHYDROUS ALCOHOL (BIOETHANOL)
"DRYMOL" PROCESS
The most attractive and least expensive technique to dehydrate water-alcohol mixtures with
concentrations in region from 93 to 96% vol. This method uses the adsorption of water in vapour phase by
means of molecular sieves using a PSA (pressure-swing-adsorption) procedure. It is able to reach
alcoholic concentrations of up to 99.9 % in volume.
Like all the adsorption operations, the separation is due to the selectivity of the adsorbent solid (zeolites)
to one of the components of the gas that crosses through it, in this case water, allowing the ethanol to
pass on and so dehydrating it.
Industrial scale PSA systems are designed to continuously repeat the cycle of pressurization/adsorption
and depressurization/de-adsorption so that the process produces a continuous flow of dehydrated alcohol.
This is possible by means of the using two or more zeolite reactors operating in an alternating fashion.
PROYECTO/PROJECT:
Planta de alcohol Superfino de Melazas
(Llave en mano)
Molasses Superfine Alcohol Plant (Turn-Key)
CAPACIDAD / CAPACITY:
90.000 Lt /dia
90,000 Lt./day
CLIENTE / CUSTOMER :
ALFICSA S.A.
Cienfuegos
CUBA
AÑO FABRICACION / YEAR :
2000
PROYECTO/PROJECT:
Planta de alcohol Superfino de Cereales
Molasses Superfine Alcohol Plant
CAPACIDAD / CAPACITY:
15.000 Lt /dia
15,000 Lt./day
CLIENTE / CUSTOMER :
GERMANY S.A.
Bucarest
RUMANIA
AÑO FABRICACION / YEAR :
1997
PROYECTO/PROJECT:
Planta de Fermentacion de Melazas, Caldera y T.Refrigeración
Molasses Alcohol Fermentation Plant, Boiler & Cooling Tower
CAPACIDAD / CAPACITY:
30.000 Lt /dia
30,000 Lt./day
CLIENTE / CUSTOMER :
SOTRAMEG S.A.
Kenitra
MARRUECOS
AÑO FABRICACION / YEAR :
1999
PROYECTO/PROJECT:
Planta de Hidrólisis y Sacarificacion de Agave (Tequila)
Hydrolisis & Saccharification Plant of Agave (Tequila)
CAPACIDAD / CAPACITY:
400.000 Kg/dia
400,000 Kg/day
CLIENTE / CUSTOMER :
CASA CUERVO S.A.
Jalisco
MEXICO
AÑO FABRICACION / YEAR :
2000
ADOLFO FDEZ. ALBARES
ÁGAVE DISTILLERIES
AGRALCO
AGROCOMERCE
AGROPAC
AGRUP. ALC. BODEGAS COOP
ALCALIBER
ALCOHOLERA CHIBCHÓN
ALCOHOLERA DE ALMENDRALEJO
ALCOHOLERA DEL PUERTO
ALCOHOLERA PONCE OLMEDA
ALCOHOLERA SAN ISIDRO
ALCOHOL. VIN. DEL MEDITERRÁNEO
ALCOHOLERAS REUNIDAS
ALCOHOLES ANTICH S.A.
ALCOHOLES DE CANARIAS
ALCOHOLES DE HUELVA
ALCOHOLES DE TOMELLOSO
ALCOHOLES DE VALENCIA
ALCOHOLES DEL PORTILLO
ALCOHOLES PONS HERMANOS
ALCOHOLES VILLAFRANCA
ALCOHOLES Y DERIVADOS
ALCOHOLES Y DERIVADOS S.A.
ALCOHOLES Y DERIV. DEL VINO
ALCOHOLES Y GRASAS DE YECLA
ALCOHOLES Y VINOS
ALCOMASA
ALDEVISA
ALFICSA
ALGRY
ALITA
ALSAN
ALVIRESA
ANIS CASTELLANA
ANIS EL MONO
ANTICH S.A.
ANTONIO VALDERA
APV BAKER IBÉRICA
ASTUR PHARMA
AZUCARERA DEL CARMEN
AZUCARERA DEL GUADALFEO
AZUCARERA EBRO AGRÍCOLA
AZUCARERA MONTERO
AZUCARERA ONÉSIMO REDONDO
AZÚCARES Y ALCOHOLES
BARCELÓ Y CÍA. CXA
BEECHAM
BEPRONA
BERE SPIRT
BIOTECNOLOGÍAS APLICADAS
BODEGAS IGLESIAS
BODEGAS MONTBLANCHI, S.A.
BODEGAS MONTERO
BOD. ORTIZ Y FERNANDO DE TERRY
BODGAS PABLO MARTÍNEZ S.A.
BODEGAS Y DESTILERÍAS
BRUGAL & CO. CXA
CAMPARI
CARLE Y MONTANARI
SPAIN
SUDÁFRICA
SPAIN
BULGARIA
MOROCCO
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
PANAMÁ
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
CUBA
SPAIN
LITUANIA
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
PANAMÁ
REP. DOM.
SPAIN
SPAIN
RUMANÍA
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
REP. DOM.
SPAIN
SPAIN
CASA CUERVO
CASA MADERO
CTRO. DE ALCOHOLES DEL PENEDÉS
CERAS INDUSTRIALES
CÉSAR PEREIRA
CÍA. LICORERA DE NICARAGUA
CISSA
CIVINASA
CLEMENTE CUESTA
CLESA
COMPAÑÍA DE INDUSTRIAS AGRÍCOLAS
CONSTAIN
CONSTRUCCIONES VENTO
COOP. DE BEZIERS
COOP. DE CIUDAD REAL
COOP. COMARCAL VALLE DE ALBAIDA
COOP. DEL CAMPO NUEVA ALCOHOL.
COOP. VINÍCOLA REQUENENSE
COVALSA
COVEN
COVIÑAS
CRUZ CONDE
CUBALCOHOL
CUBAS DE ROBLE
DECOINSA
DE SMET
DELTOSA
DESTILERÍA CHINCHÓN
DESTILERÍA DE GUADALUPE
DESTILERÍA DE MURCIA
DESTILERÍA SERRALLES
DESTILERÍAS BENITO TORRES
DESTILERÍAS DANUBIO
DESTILERÍAS DE MURICA S.A.
DESTILERÍAS DE OCCIDENTE
DESTILERÍAS DE TOMELLOSO
DESTILERÍAS DEL GUADALETE S.L.
DESTILERÍAS LOS CAMICHINES
DESTILERÍAS M.G.
DESTILERÍAS MAGISA
DESTILERÍAS PERUANAS
DESTILERÍAS SALAS Y SIRVENT
DESTILERÍAS SYS
DESTIL. Y CRIANZAS DEL WHISKY
DIEGO LÓPEZ GARCÍA-GALLO
DEULEP
DUPERIAL
EMPE S.A.
EMPRESA DE LICORES DEL ESTADO
ENGRACIO MOLLEJO MOLLEJO
ESCUELA T.S. INGENIEROS IND.
ETTEHADIED COMPANY
EUROCIENCIA
FÁBRICA NACIONAL LICORES
FAQUIRESA
FELIPE ESPINOSA S.A.
FERNANDO CALAVID
FERROVIAL
FINOS DE ÁGAVE
FLESUR
FLORIDO HERMANOS
MÉXICO
MÉXICO
SPAIN
SPAIN
PANAMÁ
NICARAGUA
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
ECUADOR
SPAIN
FRANCE
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
CUBA
ARGENTINA
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
PUERTO RICO
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
MÉXICO
SPAIN
SPAIN
PERÚ
SPAIN
SPAIN
SPAIN
SPAIN
FRANCE
ARGENTINA
SPAIN
ECUADOR
SPAIN
SPAIN
IRÁN
SPAIN
COSTA RICA
SPAIN
SPAIN
SPAIN
SPAIN
MÉXICO
SPAIN
SPAIN
FRADEALCO
FRANCISCO ARRANZ S.A.
FRANCISCO CANTARERO
FRANCISCO FERREIRA CALHAU
GINÉS NAVAROO
GLOBAL TRADE GMBH
GONZÁLEZ BYASS
GRANDES BODEGAS
HERCESA
HERMANOS TORRES
HIJOS DE FELIPE TORRES
HIJOS DE J. ANTONIO PEINADO
HIJOS DE V. CASAJUANA
HIRAM WALKER EUROPA
HUERTAS
INCAMASA
IND. DE LICORES DEL VALLE
INDUSTRIAL MAQUEDA S.A.
IND. RIBERA ANICOBA
INGENIO SAN NICOLÁS
INGENIO S. SEBASTIÁN
INSTITUTO NAL. DE INVESTIG.
ISAÍAS FUENTES
JAIME SOLER FIGUERAS
JAIME VILA MONTANA
JAVIER BALBUENA
JESÚS RAMÍREZ
JOAQUÍN CAMACHO Gª FILOSO
JOAQUÍN P. BUSTILLO
JONAS TORRES Y CÍA
JUAN JOSÉ ORTIZ
JULIÁN CHIVITE
JULIÁN MAYORDOMO POZO
JULIÁN PICAZO
JUSTO MERINO
LABORATORIOS LEO
LABORATORIOS MADE
LARIOS
LARIOS
LENSA
LIADE
LICORES DEL NORTE SANTANDER
LICORESA
LILLY
LORENZO ALCÁNTARA
MANUEL Gª DE LA CRUZ
MANUEL V. LADRÓN DE GUEVARA
MAQUIMPORT
MAREX
MINAS DE ALMADÉN
MINAZ
MODERN CHEMICAL INDUSTRIES
MOSTOS ESPAÑOLES S.A.
NAVIDUL
NUEVA ALC. DE UTIEL
OLIVARERA EXTREMEÑA
ORENDAIN
OVIONES S.A.
PEDRO DOMECQ
PEDRO DOMECQ
PEDRO DOMECQ COLOMBIA
PEDRO MARCOS MIÑAMBRES
ARGENTINA
SPAIN
SPAIN
PORTUGAL
SPAIN
GERMANY
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
COLOMBIA
SPAIN
SPAIN
MEXICO
MÉXICO
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
ECUADOR
SPAIN
SPAIN
SPAIN
COLOMBIA
ECUADOR
SPAIN
SPAIN
SPAIN
SPAIN
CUBA
RUMANÍA
SPAIN
CUBA
IRAK
SPAIN
SPAIN
SPAIN
SPAIN
MEXICO
PORTUGAL
SPAIN
MÉXICO
COLOMBIA
SPAIN
PERFUMERIE GANDUR S.A.
PIESA
PINNACLE
POLINAT
PRACSA
PRODUCTOS DE LA VID, S.A.
PRODUCTOS FINOS DE ÁGAVE
PROMARC S.L.
RAJSHREE SUGARS& CHEMICALS LTD
RAFAEL CRUZ CONCE S.A.
RAFAEL VILLEGAS
REVELANCE
RODRÍGUEZ Y BERGER
RON BERMÚDEZ
ROM PAMPERO
S.C. ALCOROM
S.C. AVIPO EUROINVEST
S.C. GERMANY SANKT PETERS.
S.C. TUNGAL METROU
S.C. VINAALCOOL ARAD
SALAS Y SIRVENT S.L..
SÁNCHEZ MONTALVO S.A.
SANIVO
SCOTT ROGER&NIXON S.A.
SEMINSA
SOC. GEN. AZUCARERA ESP.
SODEVI
SOGABINI
SOTRAMEG
SUCESOR DE HIJOS DE P. VELA
SUCROMILLES
SURANES
TABORA S.A.
TARCAL
TARCOL
TEQUILA CAZADORES
TEQUILERA DON ROBERTO
THAY ALCOHOL COMPANY
TEQUILA HERRADURA
TEQUILA SAUZA
TOLSA
TRANSFORMACIÓN DE ADITIVOS
TUCSUCO, TUY HOA
U.S.F. BEKOX
UNIÓN ALCOHOL. ESPAÑOLA
UP- JOHN
UTECO
VATRON Y MAU
VDA. ESTEBAN BOZZANO
VDA. FELIPE ESPINOSA
VDA. GONZALO FERNÁNDEZ
VDA. JOAQUÍN ORTEGA
VINAGRES PARRA
VINÍCOLA DE CHANTADA
VINÍCOLA DEL OESTE
VINÍCOLA MANCHEGA
VINÍCOLA ZAMORANA
VINTBASA
VINUMAR
VINURI SI BAUTURI HARGUITA
VIUDA DE CIPRIANO GARCÍA
WESTIM
XAMAI
SENEGAL
BULGARIA
PAKISTÁN
SPAIN
SPAIN
SPAIN
MEXICO
SPAIN
INDIA
SPAIN
SPAIN
SPAIN
SPAIN
REP. DOM.
VENEZUELA
RUMANÍA
RUMANÍA
RUMANÍA
RUMANÍA
RUMANÍA
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
PORTUGAL
SPAIN
MARRUECOS
SPAIN
COLOMBIA
SPAIN
SPAIN
ARGENTINA
ARGENTINA
MÉXICO
MÉXICO
THAILANDIA
MÉXICO
MÉXICO
SPAIN
SPAIN
VIETNAM
SPAIN
SPAIN
SPAIN
SPAIN
FRANCE
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
SPAIN
RUMANÍA
SPAIN
RUMANÍA
MÉXICO
Basic Engineering
Detailed Engineering
Construction
Erection
Supply
Supervision of erection
Commisioning supply
Feasibility study
CLIENT
Pedro Domecq Colombia S.A.
S.C. Germany Sankt Pretergurg Pr.
Promarc S.L.
S.C. Vinalcohol Arad
Global Trade GmbH
Transformación de Aditivos S.A.
Sotrameg
Destillerías del Penedés S.A.
Pedro Domecq Colombia S.A.
Minaz
Westin
Vinuri si Buturi Harguita
Transformación de Aditivos S.A.
Alficsa
Alita
SC Alcorom S.A.
Euroavipo
Biotecnologías Aplicadas S.A.
S.C. Tungal Metrou S.A.
S.C. Alcorom S.A.
Revelance S.A.
Cubalcohol
Alficsa
Sotrameg
Casa Cuervo
Orendain
Sotrameg
Casa Cuervo
Marex
Sotrameg
Sotrameg
Decoinsa
Ingenio San Nicolas
Agave Distillers
Deulep
Eurociencia S.A.
Tequila Cazadores S.A.
Tequila Herradura S.A.
Tequilera Don Roberto
Biotecnologías Aplicadas S.A.
Productos finos de Agave S.A.
Lilly S.A.
Seminsa
S.C. Bere Spirt Turnu Severin S.A.
Tequilera Don Roberto
Biotecnologías Aplicadas S.A.
Agropac
Agropac
Xamay S.A. de C.V.
Tequila Sauza S.A. de C.V.
Revelance S.A.
Tucsuco
Xuan Loc
Tarcol S.A.
Polifenoles Naturales S.L.
Ettehadieh Company
COUNTRY
Colombia
Rumania
Spain
Rumania
Germany
Spain
Morrocco
Spain
Colombia
Cuba
Rumania
Rumania
Spain
Cuba
Lituania
Rumania
Rumania
Spain
Rumania
Rumania
Spain
Cuba
Cuba
Morrocco
Mexico
Mexico
Morrocco
Mexico
Rumania
Morrocco
Morrocco
Spain
Mexico
South Africa
France
Spain
Mexico
Mexico
Mexico
Spain
Mexico
Spain
Spain
Rumania
Mexico
Spain
Morrocco
Morrocco
Mexico
Mexico
Spain
Vietnam
Vietnam
Argentina
Spain
Iran
PROJECT
2 Pot still for brandy distillation,
Grain Alcohol distillery, vacuum process. Capacity. 15.000 lt/day.
Metallic grills for security
Alcohol plant reform, from discontinued to continued. Capacity: 8.000 lt/day.
Isopropapol distillery plant. Capacity: 950.000 lt/day.
Scrubber column for alcohol recovery.
Alcohol fermentation plant for Molasses. Capacity: 30.000 lts/day
Alcohol recovery by vent in sotrage tanks. Capacity: 1.000 m3
2 Pot still for brandy distillation,
Copper column for molasses liquor production. Capacity: 35.000 lt/day.
Columns for grain neutral alcohol production using corn as feedstock.Capacity: 10,000 lt/day.
Pot still for brandy distillation.
Multiple effect evaportor for vinasses depuration. 20.000 Kg/hr evaporated water
Complete alcohol plant, vacuum system using sugar cane molasses as feedstock.Capacity: 90,000 lt/day.
Pot still for liquor production, using corn as feedstock.
Complete grain alcohol plant, vacuum system using corn as feedstock.Capacity: 15,000 lt/day.
Complete grain alcohol plant. Atmospheric pressure system using corn as feedstock.
Reactors plant reform.
Grain Alcohol distillery. Atmospheric pressure system. Capacity: 8.000 lt/day
Heat recuperator from vinasses´s distillery for heating system.
Reactor with agitator. Capacity: 2.000 lt
Fertirigation system to reuse the vinasses from distillery.
Computational control process for completed alcohol plant. Predicted adapted system.
Heat recuperator from vinasses´s distillery for 535.000 kcal/day boiler
Distillery for agave liquor (tequila). Production: 25.000 lt/day
Cooler system for agave fermentation. Capacity: 140.000 kcal/h
Water treatment system for boiler. Capacity: 8.000 lt/hr
Plant to extract agave juice by Diffusion for tequila production (500 Tn/day)
Maize cooker for hydrolysis and sacharification. Volume: 37.5 m3
Adaptive predective digital distrBIuted control system, for alcohol distillation plant.
Expansion for distillation columns. Capacity: 30.000 lt/day
Evaporation and deodorization pilot plant for purines (200 kg/h)
Installation project for fire protection
Agave´s liquor (tequila) distillery. Production: 100.000 lt/day
Anhydrous alcohol plant, molecular sieve. Production: 100.000 lt/day
Biological digestor pilot plant, and water treatment plant by inverse oSEosis
Plant for agave juice extraction by diffusion for tequila production (400 Tn/day)
Plant for agave juice extraction by diffusion for tequila production (400 Tn/day)
Plant for agave juice extraction by diffusion. (400 Tn/day)
Reactor-decanter
Plant for agave juice extraction by diffusion for tequila production (200 Tn/day)
Depuration plant for pharmaceutical resDIues. Turn-key.
Two 300m2 water tanks for fire protection
Grain Alcohol Distillation Plant for 20.000 lt/day of pure alcohol.
Distillation column for agave´s liquor (tequila). Production: 40.000 lt/day
Biological reactors.
Water treatment plant for boilers.
Essentials oils distillation plant
Agave juice extraction plant by diffusion (200Tn/day)
Agave juice extraction plant by diffusion (400Tn/day)
Deposit with agitator.
Complete plant for alcohol distillation. Capacity: 20.000 ñt/day
Complete plant for alcohol distillation. Using cassava as feedstock. Capacity: 20.000 lt/day.
Extraction diffuser of tartrates, from grapes mash. Capacity: 400 tn/day.
Polifenoles extraction plant.
Engineering for molasses fermentation and distillation plant Capacity: 20 000 lt/day
LEGEND
(Modality)
BI
DI
C
E
SU
SE
CM
FS
MODALITY
BI-DI-C
BI-DI-C-SE-CM
C
BI-DI-C
TURN-KEY
DI-C-M-CM
BI-DI-C-SE-CM
BI-DI-C
BI-DI-C
BI-DI-C
BI-DI-C-SE-CM
BI-DI-C
TURN-KEY
TURN-KEY
BI-DI-C
TURN-KEY
TURN-KEY
M
BI-IC-SE-CM
BI-DI-C
BI-DI-C
SU
TURN-KEY
BI-DI-C
BI-DI-C-SE-CM
BI-DI-C
SU
BI-DI-C-SE-CM
BI-DI-C
TURN-KEY
BI-DI-C-SE-CM
TURN-KEY
BI-DI
BI-DI-C-SE-CM
BI-DI-C-SE-CM
DI-C
BI-DI-C-SE-CM
BI-DI-C-SE-CM
TURN-KEY
BI-DI-C
BI-DI-C-SE-CM
TURN-KEY
DI-C
BI-DI-C-SE-CM
BI-DI-C-SE-CM
DI-C
SU
BI-DI-C
TURN-KEY
TURN-KEY
DI-C-M-CM
TURN-KEY
BI-DI-C-SE-CM
BI-DI-C-SE-CM
BI-DI-C-SE-CM
BI-DI-SE-CM
YEAR
1.997
1.997
1.997
1.997
1.997
1.997
1.997
1.997
1.998
1.998
1.998
1.998
1.998
1.998
1.998
1.998
1.998
1.998
1.998
1.998
1.999
1.999
1.999
1.999
1.999
1.999
1.999
2.000
2.000
2.000
2.000
2.000
2.000
2.000
2.001
2.001
2.001
2.001
2.001
2.001
2.001
2.002
2.002
2.002
2.002
2.002
2.002
2.002
2.002
2.003
2.003
2.003
2.003
2.003
2.003
2 003
Avda. de Aragón, 336, Edif. 6
28022-Madrid
Spain
Tel.:34.913294938
Fax: 34.913292467
E-mail: tomsadestil@terra.es
www.tomsa.es