Resumes
Resumes
Jack Lonsinger
View pageWork:
Liberty Carbon Service Inc
Owner
Owner
Jack Lonsinger Phones & Addresses
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1706 Johnson Industrial Dr, Excelsior Springs, MO 64024
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508 Clayview Dr, Liberty, MO 64068
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513 N Ridge Ave, Liberty, MO 64068
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Chillicothe, MO
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Clay, MO
Work
Company:
Liberty carbon service inc
Position:
Owner
Business Records
Name / Title
Company / Classification
Phones & Addresses
Partner
Liberty Carbon Service Inc
Chemicals · Mfg Industrial Inorganic Chemicals Whol Plumbing Equipment/Supplies
Chemicals · Mfg Industrial Inorganic Chemicals Whol Plumbing Equipment/Supplies
1706 Johnson Industrial D, Excelsior Springs, MO 64024
1706 Johnson Industrial Dr, Excelsior Springs, MO 64024
(816) 630-6575, (816) 630-4549
1706 Johnson Industrial Dr, Excelsior Springs, MO 64024
(816) 630-6575, (816) 630-4549
Publications
Us Patents
Production Of Thiosemicarbazide
View pageUS Patent:
42566614, Mar 17, 1981
Filed:
Nov 1, 1979
Appl. No.:
6/090213
Inventors:
Danny B. Barton - Kansas City MO
Chester W. Halbleib - Holt MO
Jack J. Lonsinger - Liberty MO
Chester W. Halbleib - Holt MO
Jack J. Lonsinger - Liberty MO
Assignee:
Mobay Chemical Corporation - NJ
International Classification:
C07C15900
US Classification:
564 18
Abstract:
In the production of thiosemicarbazide comprising the steps of reacting hydrazine and ammonium thiocyanate to form hydrazinium thiocyanate and by-product ammonia, and heating the hydrazinium thiocyanate to effect isomerization thereof to thiosemicarbazide, the improvement which comprises removing the ammonia from the hydrazinium thiocyanate prior to isomerization thereof, whereby the thiosemicarbazide is produced in high yield and purity. Advantageously at least about 80% of the ammonia is removed by steam stripping and/or vacuum distillation and the subsequent isomerization is effected by prolonged heating in the presence of a carbonyl compound such as acetone or acetaldehyde. The thiosemicarbazide is recovered by cooling to effect crystallization, followed by filtration, the mother liquor being recycled as solvent medium for the next batch.
Method Of Reducing Carbon Loss In Regeneration Process
View pageUS Patent:
50136984, May 7, 1991
Filed:
Dec 27, 1989
Appl. No.:
7/457395
Inventors:
Deborah A. Lonsinger - Liberty MO
Jack J. Lonsinger - Liberty MO
Jack J. Lonsinger - Liberty MO
International Classification:
B01J 2034
B01J 3860
C02F 142
B01J 3860
C02F 142
US Classification:
502 27
Abstract:
A method of reducing alkaline earth metals contamination of activated carbon by washing the contaminated product with an inorganic acid, preferably hydrochloric, and then rinsing the acid washed carbon with water. Preferably, the washing step is carried out from three to thirty minutes at a pH of 2. 5 or less. The rinsing step is continued until a pH of 5 or greater is obtained, preferably for a time period of at least three to five minutes. The method is applicable to any alkaline earth metal but particularly calcium and magnesium. Any inorganic may be employed with those forming water soluble salts being preferred. The invention also encompasses a method of regenerating spent activated carbon employing the acid wash and rinsing steps noted above followed by separating the washed carbon from the rinse water followed by drying and then pyrolizing the dried carbon at a temperature of approximately 500 degrees C. to 1100 degrees C. so as to effect the water gas reaction.
Preparation Of O,S-Dialkyl Phosphoroamidothioates
View pageUS Patent:
43893503, Jun 21, 1983
Filed:
May 19, 1981
Appl. No.:
6/265046
Inventors:
Jack J. Lonsinger - Liberty MO
Chester W. Halbleib - Holt MO
Chester W. Halbleib - Holt MO
Assignee:
Mobay Chemical Corporation - Kansas City MO
International Classification:
C07F 924
US Classification:
260989
Abstract:
In the isomerization of an O,O-dialkyl phosphoroamidothioate to an O,S-dialkyl phosphoroamidothioate by heating the O,O-dialkyl starting material in the presence of a catalyst, followed by recovery of the desired O,S-dialkyl end product, the improvement which comprises arresting the heating when about 40 to 70% of the O,O-dialkyl starting material has isomerized to O,S-dialkyl product, separating unreacted O,O-dialkyl starting material from the O,S-dialkyl isomerization product, and further treating the O,O-dialkyl starting material to effect further isomerization. The separation is effected either by cooling to crystallize out O,S-dialkyl isomer or by evaporating off the O,O-dialkyl starting material.
Process For Regeneration Of Activated Carbon
View pageUS Patent:
49577212, Sep 18, 1990
Filed:
Jun 28, 1988
Appl. No.:
7/212610
Inventors:
Jack J. Lonsinger - Liberty MO
Deborah A. Lonsinger - Liberty MO
Deborah A. Lonsinger - Liberty MO
International Classification:
C01B 3102
US Classification:
423461
Abstract:
A method and apparatus for reactivating spent granular activated carbon is the subject of this invention. The carbonaceous material is to be activated is fed to a drying zone where it is dried until incoming air and recycle gases fluidize the drying zone thus causing the dried material to be pneumatically conveyed to the regeneration or activation zone. In this zone, the temperature is raised to effect the oxidizing reactions thereby volatilizing at least some of the contaminants while converting residual carbon to carbon monoxide and hydrogen. Some of the produce gases from the drying and regeneration zones are utilized to fluidize both of these zones and the remaining gases are directed to the afterburner where combustibles are consumed. The product gases from the afterburner are then directed to a conditioning zone where combustible fuel is introduced so as to consume any residual oxygen. The conditioned gas is then recycled to the regeneration zone where it fluidizes the regenerated produce which is then pneumatically conveyed out of the regenerator container.