EP1010752A1 - Unique multifunctional product for detergent formulations - Google Patents

Unique multifunctional product for detergent formulations Download PDF

Info

Publication number
EP1010752A1
EP1010752A1 EP98931108A EP98931108A EP1010752A1 EP 1010752 A1 EP1010752 A1 EP 1010752A1 EP 98931108 A EP98931108 A EP 98931108A EP 98931108 A EP98931108 A EP 98931108A EP 1010752 A1 EP1010752 A1 EP 1010752A1
Authority
EP
European Patent Office
Prior art keywords
product
detergent
detergent formulations
raw materials
single product
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.)
Withdrawn
Application number
EP98931108A
Other languages
German (de)
English (en)
French (fr)
Inventor
Enrique Hernandez Torres-Landa
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Vitro Corporativo SA de CV
Original Assignee
Vitro Corporativo SA de CV
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 Vitro Corporativo SA de CV filed Critical Vitro Corporativo SA de CV
Publication of EP1010752A1 publication Critical patent/EP1010752A1/en
Withdrawn legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D11/00Special methods for preparing compositions containing mixtures of detergents
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02Inorganic compounds
    • C11D7/04Water-soluble compounds
    • C11D7/10Salts
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02Inorganic compounds
    • C11D7/04Water-soluble compounds
    • C11D7/10Salts
    • C11D7/14Silicates
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02Inorganic compounds
    • C11D7/04Water-soluble compounds
    • C11D7/10Salts
    • C11D7/16Phosphates including polyphosphates

Definitions

  • This invention refers to a multifunctional single product for detergent formulations, and more particularly, to a product in the form of a powder or a glass, which is water soluble and acts as builder, conditioner, filler and carrier, among others, in the detergent and in the process for its manufacture.
  • phosphorus oxide P 2 O 5
  • sodium oxide Na 2 O
  • silica SiO 2
  • B 2 O 3 boron oxide
  • These oxides are normally provided through a plurality of raw materials or chemical compounds, such as the sodium carbonate (Na 2 CO 3 ), sodium tripolyphosphate (Na 5 P 3 O 10 ), sodium sulfate (Na 2 SO 4 ), sodium silicate (xNa 2 O ⁇ ySiO 2 ) and sodium borate (Na 2 B 4 O 7 ).
  • sodium carbonate Na 2 CO 3
  • sodium tripolyphosphate Na 5 P 3 O 10
  • sodium sulfate Na 2 SO 4
  • sodium silicate xNa 2 O ⁇ ySiO 2
  • sodium borate Na 2 B 4 O 7
  • each detergent producer has its own formulations, but each producer normally buys and uses the above-mentioned typical chemical compounds as raw materials.
  • each of such compounds performs a task, acting as a builder, as a conditioner, as a filler, as a carrier, as a neutralizing agent, etc. in the detergent and /or in the process for its manufacture.
  • the sodium tripolyphosphate a raw material normally used in the detergent formulation as a source of phosphorus oxide (P 2 O 5 ), is made by reacting phosphoric acid with sodium carbonate; that in turn, the phosphoric acid is obtained from the reaction of the grounded phosphoric rock with sulfuric acid, which is filtered for impurity elimination which is not but silica which is also present in the detergent formulation; and that the sodium carbonate is normally obtained by a process for the benefitiation of the trona ore by impurity elimination which is not but silica which is also present in the detergent formulations.
  • the impurity compounds are also materials present in the detergent formulations, and that the process for their elimination add a cost to the raw materials and consequently to the final detergent, then the mineral treatment to obtain such raw materials becomes unnecessary and the phosphoric rock or at least the phosphoric acid can be used, through just a partial treatment (such as acid or alkaline attack, as well as grounding, sieving and screening), to produce a product which would be used as a source of P 2 O 5 and as a partial source of SiO 2 in the detergent formulations.
  • a partial treatment such as acid or alkaline attack, as well as grounding, sieving and screening
  • the Na 2 O is provided through the sodium carbonate obtained from the treatment of trona mineral by a process including grounding, diluting, filtering to eliminate compounds considered as impurities (which are compounds also used in the detergent formulations) and crystallizing, to obtain the sodium carbonate.
  • trona mineral could be used directly, through a simple grounding step, at more reduced costs, to prepare a single product which would be adjusted to the detergent formulation needs.
  • the SiO 2 is provided through the sodium silicate which is obtained from reacting silica sand and sodium carbonate in a furnace.
  • the multifunctional product developed by applicants will provide the silica that the detergent formulation needs.
  • the detergent producer will have not the need to buy 5 or 8 different raw materials for its formulation, but a single product which is less expensive because it will not include the costs of the purifying processes incorporated in each raw material and because such a product involves just one process, instead of each process to produce each of the actual raw materials.
  • This product will provide the oxide needs for the detergent formulation and for its manufacturing process and will perform the essential roles or functions such as builder, conditioner, filler, carrier, neutralizing agent, etc. in detergent formulations and in its manufacturing process.
  • This product can also be used in the processes for producing detergents, instead of all the raw materials used in the conventional processes, to achieve each of the roles or functions as builder, carrier, filler, among others.
  • the obtained product is soluble in water and it will perform the essential roles or functions such as builder, conditioner, filler, carrier, etc. in detergent formulations and in its manufacturing process and results less expensive than the raw materials normally used.
  • the detergent producers changed their process technology to produce detergents in the tower process and in the agglomerate process. In both cases they needed almost the same type of raw materials, however they needed solid and liquid raw materials such as sodium tripolyphosphate and sodium silicate.
  • solid and liquid raw materials such as sodium tripolyphosphate and sodium silicate.
  • the detergent producer does not have to pay for multiple raw material handling and transportation, nor to pay for transporting some unneeded volatile or gaseous components such as the CO 2 , that are present in the raw materials used such as in the sodium carbonate.
  • the reacting step is carried out either, at a temperature under the melting point of the mixture, to produce a powder, or at a reacting and melting temperature of the mixture, to provide a glass.
  • the process comprising to dissolve the powder or the glass product in a solvent, to produce a liquid product including most of the typical oxides normally included in the detergent formulations.
  • a final annealing step for the product can be introduced in the process.
  • the single reacted product, in accordance with the present invention include the essential oxides, such as phosphorus oxide (P 2 O 5 ), sodium oxide (Na 2 O), silica (SiO 2 ), balanced in accordance with the specific detergent formulations, which is water soluble and performs as builder, conditioner, filter, carrier and neutralizing agent, in the product and in the process for the manufacturing of the detergent.
  • the essential oxides such as phosphorus oxide (P 2 O 5 ), sodium oxide (Na 2 O), silica (SiO 2 )
  • the specific detergent formulations which is water soluble and performs as builder, conditioner, filter, carrier and neutralizing agent, in the product and in the process for the manufacturing of the detergent.
  • the final oxide content of the product of the present invention will depend on the type and oxide content of the detergent formulation, which detergent producers normally keep secret.
  • This batch 5 was reacted in a rotary kiln K at a temperature of about 800°C and then the reacted batch 6 was fed to a furnace F to melt the reacted batch 6 at a temperature of about 1200°C, to produce one ton of a glass product 7.
  • This batch 5 was reacted in a rotary kiln K at a temperature of about 800°C and then the reacted batch 6 was fed to a furnace F to melt the batch 6 at a temperature of about 1200°C, to produce one ton of a glass product 7.
  • the sodium carbonate from the feeder 1a and the silica sand from the feeder 2 were feed to a mixer M to homogenize the primary raw materials; the mixture 3 was then introduced into an agglomerator A to which the phosphoric acid 4a was added to agglomerate these raw materials to produce a batch 5 in the following ratio 1P 2 O 5 : 4Na 2 O : 4 SiO 2 .
  • This batch 5 was directly reacted in the furnace F to melt the batch 5 at a temperature of about 1200°C, to produce one ton of a glass product 7.
  • sodium sulfate from a feeder 8 was directly added, in an amount of 10% by weight, to the mixer M containing the natural or partially treated raw materials of the Examples 1 to 3, reacted in the kiln K and melted in the furnace F in accordance with Examples 1 and 2, or directly reacted and melted in the furnace F in accordance with the Example 3, at the same temperature than the above examples, to produce a glass product 7a.
  • the glass product 7 from Examples 1 to 3 or 7a from the Example 4 was fed to mill ML, milled therein and the milled mixture 9 was fed to a mixer M2 in which an additional amount of sodium sulfate from a feeder 8a was added to milled mixture 9, in a double amount of the weight of the product 7 or 7a, to obtain the product 7b.
  • Grounded trona ore from feeder 1 and silica sand from feeder 2 were feed to the mixer M to homogenize the primary raw materials; the mixture 3 was then introduced into the agglomerator A in which treated (acid attacked) phosphoric rock from feeder 4 was added to agglomerate these raw materials to produce a batch 5 in the following ratio 1P 2 O 5 : 4Na 2 O : 4 SiO 2 .
  • This batch 5 was directly reacted in the rotary kiln K at a temperature of about 700°C to produce a powder product 7c.
  • the product 7 or 7a of Examples 1 to 4, or 7c of the Example 6 was dissolved in water, at a temperature of 90°C in a dissolver D, to produce a liquid product 7d having a concentration of 33% of the total product.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Detergent Compositions (AREA)
EP98931108A 1997-07-09 1998-06-17 Unique multifunctional product for detergent formulations Withdrawn EP1010752A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US89012197A 1997-07-09 1997-07-09
US890121 1997-07-09
PCT/MX1998/000023 WO1999002643A1 (es) 1997-07-09 1998-06-17 Un solo producto multifunctional para formulaciones de detergente

Publications (1)

Publication Number Publication Date
EP1010752A1 true EP1010752A1 (en) 2000-06-21

Family

ID=25396286

Family Applications (1)

Application Number Title Priority Date Filing Date
EP98931108A Withdrawn EP1010752A1 (en) 1997-07-09 1998-06-17 Unique multifunctional product for detergent formulations

Country Status (15)

Country Link
EP (1) EP1010752A1 (pt)
JP (1) JPH11106787A (pt)
CN (1) CN1262704A (pt)
AR (1) AR013187A1 (pt)
BR (1) BR9810987A (pt)
CA (1) CA2295702A1 (pt)
CO (1) CO5031341A1 (pt)
EG (1) EG21669A (pt)
HU (1) HUP9801520A2 (pt)
IL (1) IL125269A (pt)
MA (1) MA24602A1 (pt)
PE (1) PE95199A1 (pt)
TR (1) TR199801307A3 (pt)
WO (1) WO1999002643A1 (pt)
ZA (1) ZA985929B (pt)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1105450A1 (en) * 1998-08-17 2001-06-13 The Procter & Gamble Company Multifunctional detergent materials
DE102004020033A1 (de) * 2004-04-21 2005-11-10 Henkel Kgaa Verbrauchsanzeiger für maschinelle Geschirrspülmittel

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001092448A2 (es) * 2000-05-31 2001-12-06 Vitro Corporativo, S.A. De C.V. Composicion de oxidos soluble en agua, para formulaciones de detergente

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3270156B2 (ja) * 1992-11-12 2002-04-02 花王株式会社 無機ビルダー
US5393446A (en) * 1992-12-16 1995-02-28 Eco Japan Co., Ltd. Process for preparing detergent composition containing sodium and potassium oxides
JPH0859225A (ja) * 1994-08-18 1996-03-05 Tokuyama Corp 非晶質珪酸カリウム粉末及びその製造方法
JPH08143309A (ja) * 1994-11-17 1996-06-04 Tokuyama Corp 非晶質珪酸ナトリウム・炭酸ナトリウム複合体の製造方法

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO9902643A1 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1105450A1 (en) * 1998-08-17 2001-06-13 The Procter & Gamble Company Multifunctional detergent materials
DE102004020033A1 (de) * 2004-04-21 2005-11-10 Henkel Kgaa Verbrauchsanzeiger für maschinelle Geschirrspülmittel

Also Published As

Publication number Publication date
CA2295702A1 (en) 1999-01-21
BR9810987A (pt) 2000-08-08
IL125269A0 (en) 1999-03-12
CN1262704A (zh) 2000-08-09
HU9801520D0 (en) 1998-08-28
PE95199A1 (es) 1999-10-14
EG21669A (en) 2002-02-27
AR013187A1 (es) 2000-12-13
IL125269A (en) 2001-08-08
ZA985929B (en) 1999-08-13
TR199801307A2 (xx) 1999-10-21
JPH11106787A (ja) 1999-04-20
HUP9801520A2 (hu) 1999-09-28
MA24602A1 (fr) 1999-04-01
CO5031341A1 (es) 2001-04-27
TR199801307A3 (tr) 1999-10-21
WO1999002643A1 (es) 1999-01-21

Similar Documents

Publication Publication Date Title
US20240190716A1 (en) Systems and Methods to Recover Value-Added Materials from Gypsum
IE52048B1 (en) Process for producing metal silicates from solutions of alkali metal silicates and use thereof in glass making
CN106517738B (zh) 用于熔融和澄清钠钙玻璃的方法
CN102002585B (zh) 一种石煤酸浸液生产钒铁合金的方法
CN109665528B (zh) 含有刚玉型石英岩制备电子产品用高纯石英砂粉的方法
CN104797537B (zh) 无碱玻璃的制造方法
WO2020154699A1 (en) Systems and methods to treat flue gas desulfurization and metal-bearing waste streams to recover value-added materials
US20210347648A1 (en) Systems and methods to treat flue gas desulfurization and metal-bearing waste streams to recover value-added materials
CN107344725A (zh) 硫酸直浸法提取锂矿石中锂元素的制备工艺
CN101905885A (zh) 一种用于提纯硅的低硼熔渣及其制备方法
JP5778342B2 (ja) アルミノホウケイ酸ガラスを原料とするa型ゼオライトの製造方法
CN111392702B (zh) 一种半水二水工艺制备浓磷酸和石膏粉的方法
EP1010752A1 (en) Unique multifunctional product for detergent formulations
CN105540623A (zh) 一种制备纳米氧化镁的方法
CN1039112C (zh) 硫酸分解硼镁铁矿综合利用工艺
EP1211229A2 (en) Method for preparing pre-reacted raw material batches for the production of glass formulae
Simon et al. Borate raw materials
CN1323908A (zh) 从氟碳铈镧精矿中制备低氟氯化稀土料液的优溶方法
CN1120803C (zh) 碱渣、钾长石制氯化钾的工艺方法
KR101021170B1 (ko) 니켈 슬래그로부터 황산을 이용한 마그네슘의 침출 및 물유리의 제조방법
WO2016148446A1 (ko) 전기로 더스트로부터 아연화합물을 제조하는 방법
CN102674410A (zh) 一种高纯氟化镁晶体的生产方法
CZ200032A3 (cs) Jediný multifunkční produkt pro receptury detergentů
CN112456545A (zh) 一种利用剥锡废液制备三水合锡酸钠的方法
JP2013142048A (ja) 無アルカリガラスを原料とするゼオライトの製造方法、a型ゼオライトおよびそれを用いた成形体、水浄化剤、土壌改質剤、保肥剤

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20000120

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): BE DE ES FR GB IT NL

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20020101